ML17033B518

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Redacted Updated Final Safety Analysis Report Chapter 5
ML17033B518
Person / Time
Site: North Anna  Dominion icon.png
Issue date: 09/29/2016
From: V Sreenivas
Plant Licensing Branch II
To: Heacock D
Virginia Electric & Power Co (VEPCO)
Sreenivas V, NRR/DORL/LPL2-1, 415-2597
Shared Package
ML17033B477 List:
References
Download: ML17033B518 (352)
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Text

North Anna Power Station Updated Final Safety Analysis Report Chapter 5

Intentionally Blank Revision 5209/29/2016 NAPS UFSAR 5-i Chapter 5: Reactor Coolant System Table of Contents Section Title Page 5.1

SUMMARY

DESCRIPTION. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-1 5.1.1 Reactor Coolant System Components. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-2 5.1.1.1 Reactor Vessel . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-2 5.1.1.2 Steam Generators. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-2 5.1.1.3 Reactor Coolant Pumps . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-2 5.1.1.4 Piping. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-3 5.1.1.5 Pressurizer . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-3 5.1.1.6 Pressurizer Relief Tank . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-3 5.1.1.7 Safety and Relief Valves . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-3 5.1.1.8 Loop Stop Valves . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-3 5.1.1.9 Reactor Vessel Head Shielding . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-3 5.1.2 Reactor Coolant System Performance and Safety Functions . . . . . . . . . . . . . . . 5.1-4 5.1.2.1 Reactor Coolant Flow . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-4 5.1.2.2 Interrelated Performance and Safety Functions. . . . . . . . . . . . . . . . . . . . . . . . 5.1-6 5.1.3 System Operation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-7 5.1.3.1 Plant Start-up . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-7 5.1.3.2 Power Generation and Hot Shutdown . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-9 5.1.3.3 Plant Shutdown . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-9 5.1.3.4 Refueling . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-10 5.1.3.5 Loss of Decay Heat Removal . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-10 5.1 References. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-13 5.1 Reference Drawings . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-13 5.2 INTEGRITY OF THE REACTOR COOLANT SYSTEM BOUNDARY . . . . . . 5.2-1 5.2.1 Design Criteria Methods and Procedures . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-1 5.2.1.1 Performance Objectives and Design Conditions . . . . . . . . . . . . . . . . . . . . . . . 5.2-1 5.2.1.2 Design Evaluation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-8 5.2.2 Overpressurization Protection . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-16 5.2.2.1 Normal Operation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-16 5.2.2.2 Start-up and Shutdown . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-17 5.2.2.3 Water-Solid Protection . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-19 5.2.2.4 Pressurized Thermal Shock . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-20 5.2.3 Material Considerations . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-20 5.2.3.1 Materials of Construction . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-20 5.2.3.2 Chemistry Control . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-28

Revision 5209/29/2016 NAPS UFSAR 5-ii Chapter 5: Reactor Coolant System Table of Contents (continued)

Section Title Page 5.2.3.3 Fracture Prevention . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-29 5.2.3.4 Cleaning and Contamination Protection . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-33 5.2.4 Reactor Coolant Pressure Boundary Leakage Detection Systems . . . . . . . . . . . 5.2-35 5.2.4.1 Leakage to the Containment . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-35 5.2.4.2 N-16 Primary to Secondary Leakage Detection System . . . . . . . . . . . . . . . . . 5.2-39 5.2.5 Inservice Inspection Programs . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-40 5.2.5.1 Program . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-40 5.2.5.2 Inservice Inspection Equipment . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-43 5.2.5.3 Loose Parts Monitoring . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-43 5.2.5.4 Vibration Monitoring. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-44 5.2 References. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-45 5.3 THERMAL-HYDRAULIC SYSTEM DESIGN . . . . . . . . . . . . . . . . . . . . . . . . . . 5.3-1 5.4 REACTOR VESSEL AND APPURTENANCES . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-1 5.4.1 Design Bases . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-1 5.4.1.1 Codes and Specifications. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-1 5.4.1.2 Design Transients . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-1 5.4.1.3 Protection Against Nonductile Failure . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-1 5.4.1.4 Inspection. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-2 5.4.2 Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-2 5.4.2.1 Fabrication Processes. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-3 5.4.3 Evaluation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-4 5.4.3.1 Steady-State Stresses . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-4 5.4.3.2 Fatigue Analysis Based on Transient Stresses. . . . . . . . . . . . . . . . . . . . . . . . . 5.4-4 5.4.3.3 Thermal Stresses Due to Gamma Heating. . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-4 5.4.3.4 Thermal Stresses Due to a LOCA . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-4 5.4.3.5 Heatup and Cooldown . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-4 5.4.3.6 Irradiation Surveillance Program. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-5 5.4.3.7 Capability for Annealing the Reactor Vessel . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-11 5.4.4 Tests and Inspections . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-11 5.4.4.1 Ultrasonic Examinations . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-12 5.4.4.2 Penetrant Examinations . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-12 5.4.4.3 Magnetic Particle Examinations . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-12 5.4.4.4 Inservice Inspection . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-12

Revision 5209/29/2016 NAPS UFSAR 5-iii Chapter 5: Reactor Coolant System Table of Contents (continued)

Section Title Page 5.4 References. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-13 5.5 COMPONENT AND SUBSYSTEM DESIGN . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-1 5.5.1 Reactor Coolant Pumps. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-1 5.5.1.1 Design Bases . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-1 5.5.1.2 Design Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-1 5.5.1.3 Design Evaluation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-3 5.5.1.4 Tests and Inspections. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-8 5.5.2 Steam Generator . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-11 5.5.2.1 Design Bases . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-11 5.5.2.2 Design Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-12 5.5.2.3 Design Evaluation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-12 5.5.2.4 Tests and Inspections. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-15 5.5.3 Reactor Coolant Piping . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-16 5.5.3.1 Design Bases . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-16 5.5.3.2 Design Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-16 5.5.3.3 Design Evaluation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-19 5.5.3.4 Tests and Inspections. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-20 5.5.4 Residual Heat Removal System . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-20 5.5.4.1 Design Bases . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-20 5.5.4.2 System Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-21 5.5.4.3 Design Evaluation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-25 5.5.4.4 Tests and Inspections. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-28 5.5.5 Pressurizer . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-28 5.5.5.1 Design Bases . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-28 5.5.5.2 Design Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-29 5.5.5.3 Design Evaluation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-30 5.5.5.4 Tests and Inspections. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-33 5.5.6 Pressurizer Relief Tank . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-33 5.5.6.1 Design Bases . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-33 5.5.6.2 Design Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-33 5.5.6.3 Design Evaluation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-34 5.5.7 Valves Other Than Safety and Relief Valves . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-35 5.5.7.1 Design Bases . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-35 5.5.7.2 Design Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-35

Revision 5209/29/2016 NAPS UFSAR 5-iv Chapter 5: Reactor Coolant System Table of Contents (continued)

Section Title Page 5.5.7.3 Design Evaluation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-36 5.5.7.4 Tests and Inspections. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-37 5.5.8 Safety and Relief Valves . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-37 5.5.8.1 Design Bases . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-37 5.5.8.2 Design Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-37 5.5.8.3 Design Evaluation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-39 5.5.8.4 Tests and Inspections. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-40 5.5.9 Reactor Coolant System Equipment Supports . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-41 5.5.9.1 Design Basis . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-41 5.5.9.2 Description. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-42 5.5.9.3 Evaluation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-44 5.5.10 Reactor Coolant Vent System . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-47 5.5.10.1 Design Bases . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-47 5.5.10.2 Design Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-47 5.5.10.3 Design Evaluation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-49 5.5.10.4 Tests and Inspections. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-51 5.5 References. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-52 5.5 Reference Drawings . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-53 5.6 INSTRUMENTATION APPLICATION . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.6-1 5.6.1 Design Bases . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.6-1 5.6.2 Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.6-2 5.6.2.1 Temperature Measuring Instrumentation . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.6-2 5.6.2.2 Flow Indication . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.6-4 5.6.2.3 Pressure Indication. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.6-4 5.6.2.4 Liquid Level Indication . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.6-6 5.6.3 Evaluation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.6-7 5.6 Reference Drawings . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.6-8 Appendix 5A Discussion Between the Nuclear Regulatory Commission and Virginia Electric & Power Company on Steam Generator Lower and Reactor Coolant Pump Supports for North Anna Units No. 1 and 2 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5A-i NRC Questions and VEPCO Responses Subsequent to the VEPCO Presentation of April 13, 1976 . . . . . . . 5A Att. 1-i

Revision 5209/29/2016 NAPS UFSAR 5-v Chapter 5: Reactor Coolant System List of Tables Table Title Page Table 5.1-1 System Design and Operating Parameters . . . . . . . . . . . . . . . . . . . . . . . 5.1-15 Table 5.2-1 ASME Code Cases for Westinghouse PWR Class 1 Components . . . . 5.2-47 Table 5.2-2 ASME Code Cases for Class 1 Components . . . . . . . . . . . . . . . . . . . . . 5.2-50 Table 5.2-3 Equipment Code and Classification List . . . . . . . . . . . . . . . . . . . . . . . . 5.2-51 Table 5.2-4 Summary of Reactor Coolant System Design Transients . . . . . . . . . . . 5.2-54 Table 5.2-5 Steam Generator Primary/Secondary Boundary Components. . . . . . . . 5.2-55 Table 5.2-6 Steam Generator Primary/Secondary Boundary Components. . . . . . . . 5.2-55 Table 5.2-7 Steam Generator Primary/Secondary Boundary Components. . . . . . . . 5.2-56 Table 5.2-8 Steam Generator Primary/Secondary Boundary Components. . . . . . . . 5.2-56 Table 5.2-9 Steam Generator Primary/Secondary Boundary Components. . . . . . . . 5.2-57 Table 5.2-10 Steam Generator Primary/Secondary Boundary Components. . . . . . . . 5.2-57 Table 5.2-11 Steam Generator Primary/Secondary Boundary Components. . . . . . . . 5.2-58 Table 5.2-12 Limit Analysis Calculations Results . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-59 Table 5.2-13 Load Combinations and Operating Conditions . . . . . . . . . . . . . . . . . . . 5.2-59 Table 5.2-14 Loading Conditions and Stress Limits: Class A Components . . . . . . . . 5.2-60 Table 5.2-15 Loading Conditions and Stress Limits: Nuclear Power Pipinga . . . . . . 5.2-61 Table 5.2-16 Faulted Condition Stress Limits for Class A Components . . . . . . . . . . 5.2-62 Table 5.2-17 Faulted Condition Loads for the Reactor Coolant Pump Feet . . . . . . . . 5.2-63 Table 5.2-18 Operating and Inactive Valves in the Reactor Coolant System Boundary 5.2-64 Table 5.2-19 Active Valves in the Reactor Coolant Pressure Boundary . . . . . . . . . . 5.2-66 Table 5.2-20 RTPTS Values for North Anna Unit 1 a . . . . . . . . . . . . . . . . . . . . . . . . 5.2-67 Table 5.2-21 RTPTS Values for North Anna Unit 2 a ........................ 5.2-67 Table 5.2-22 Reactor Coolant Pressure Boundary Materials . . . . . . . . . . . . . . . . . . . 5.2-68 Table 5.2-23 Reactor Coolant Pressure Boundary Materials Auxiliary Components . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-72 Table 5.2-24 Reactor Vessel Internals for Emergency Core Cooling . . . . . . . . . . . . . 5.2-74 Table 5.2-25 Reactor Coolant Water Chemistry Specification . . . . . . . . . . . . . . . . . . 5.2-75 Table 5.2-26 Pre-irradiation Reactor Vessel Toughness Table (Unit 1) . . . . . . . . . . . 5.2-76 Table 5.2-27 Pre-irradiation Reactor Vessel Toughness Table (Unit 2) . . . . . . . . . . . 5.2-78 Table 5.2-28 Preservice Inspection Program. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-80

Revision 5209/29/2016 NAPS UFSAR 5-vi Chapter 5: Reactor Coolant System List of Tables (continued)

Table Title Page Table 5.4-1 Reactor Vessel Design Parameters . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-14 a

Table 5.4-2 Surveillance Capsule Withdrawal Schedule for North Anna Unit 1 . . 5.4-15 Table 5.4-3 Surveillance Capsule Withdrawal Schedulea for North Anna Unit 2 . . 5.4-16 Table 5.4-4 Reactor Vessel Quality Assurance Program . . . . . . . . . . . . . . . . . . . . . 5.4-17 Table 5.4-5 Reactor Vessel Closure Head Quality Assurance Program . . . . . . . . . . 5.4-18 Table 5.5-1 Reactor Coolant Pump Design Parameters . . . . . . . . . . . . . . . . . . . . . . 5.5-54 Table 5.5-2 Reactor Coolant Pump Quality Assurance Program . . . . . . . . . . . . . . . 5.5-55 Table 5.5-3 Steam Generator Design Data . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-55 Table 5.5-4 Steam Generator Quality Assurance Program . . . . . . . . . . . . . . . . . . . . 5.5-56 Table 5.5-5 Reactor Coolant Piping Design Parameters . . . . . . . . . . . . . . . . . . . . . . 5.5-57 Table 5.5-6 Reactor Coolant Thermal Sleeve Removal . . . . . . . . . . . . . . . . . . . . . . 5.5-57 Table 5.5-7 Reactor Coolant Piping Quality Assurance Program. . . . . . . . . . . . . . . 5.5-58 Table 5.5-8 Design Bases for Residual Heat Removal System Operation . . . . . . . . 5.5-58 Table 5.5-9 Residual Heat Removal System Codes and Classifications. . . . . . . . . . 5.5-59 Table 5.5-10 Residual Heat Removal System Component Data. . . . . . . . . . . . . . . . . 5.5-60 Table 5.5-11 Pressurizer Design Data . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-61 Table 5.5-12 Reactor Coolant System Design Pressure Typical Settings (psig) . . . . 5.5-61 Table 5.5-13 Pressurizer Quality Assurance Program . . . . . . . . . . . . . . . . . . . . . . . . 5.5-62 Table 5.5-14 Pressurizer Relief Tank Design Data . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-63 Table 5.5-15 Reactor Coolant System Boundary Valve Design Parameters . . . . . . . 5.5-63 Table 5.5-16 Reactor Coolant System Valve Quality Assurance Program. . . . . . . . . 5.5-64 Table 5.5-17 Pressurizer Valves Design Parameters. . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-65 Table 5.5-18 Maximum Steam Generator and Reactor Coolant Pump Foot Loads (kips) . . . . . . . . . . . . . . . . . . . . . . . 5.5-65 Table 5.5-19 Maximum Load (kips), Supports . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-66 Table 5.5-20 Maximum Load (kips), Snubbers and Struts . . . . . . . . . . . . . . . . . . . . . 5.5-66

Revision 5209/29/2016 NAPS UFSAR 5-vii Chapter 5: Reactor Coolant System List of Figures Figure Title Page Figure 5.1-1 Reactor Coolant System. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.1-16 a

Figure 5.1-2 Original Design Basis Pump Head - Flow Characteristics . . . . . . . . . 5.1-17 Figure 5.2-1 Primary-Secondary Boundary Components Shell Locations of Stress Investigations . . . . . . . . . . . . . . . . . . . . . . . 5.2-84 Figure 5.2-2 Reactor Coolant Pump Casing with Support Feet . . . . . . . . . . . . . . . . 5.2-85 Figure 5.2-3 Reactor Coolant Pump Support Feet . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-86 Figure 5.2-4 Reactor Coolant System Water Solid Operation . . . . . . . . . . . . . . . . . 5.2-87 Figure 5.2-5 Typical Reactor Coolant System Heatup Limitations Curve. . . . . . . . 5.2-88 Figure 5.2-6 Typical Reactor Coolant System Cooldown Limitations Curve . . . . . 5.2-89 Figure 5.2-7 Effect of Fluence and Copper Content on Shift of RTNDT for Reactor Vessel Steels Exposed to 550°F Temperature . . . . . . . . . 5.2-90 Figure 5.2-8 Fluence Versus Full Power Years . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-91 Figure 5.2-9 KID Lower Bound Fracture Toughness A533V (Reference WCAP 7623) Grade B Class 1 . . . . . . . . . . . . . . . . . . . . . 5.2-92 Figure 5.2-10 Corten and Sailors Correlation. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.2-93 Figure 5.2-11 Containment Radiation Monitor Sensitivities . . . . . . . . . . . . . . . . . . . 5.2-94 Figure 5.3-1 Temperature Versus Power . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.3-2 Figure 5.4-1 Reactor Vessel . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-19 Figure 5.4-2 Reactor Vessel Head . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-20 Figure 5.4-3 Specimen Guide to Thermal Shield Attachment . . . . . . . . . . . . . . . . . 5.4-21 Figure 5.4-4 Typical Surveillance Capsule Elevation View. . . . . . . . . . . . . . . . . . . 5.4-22 Figure 5.4-5 Surveillance Capsule, Plan Viewa . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.4-23 Figure 5.5-1 Reactor Coolant Pump 1-RC-P-1C . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-67 Figure 5.5-2 Reactor Coolant Pump 1-RC-P-1A & -1B; 2-RC-P-1A, 1B & -1C . . 5.5-68 Figure 5.5-3 Reactor Coolant Pump Estimated Performance Characteristic . . . . . . 5.5-69 Figure 5.5-4 51F Series Steam Generator. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-70 Figure 5.5-5 Residual Heat Removal System. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-71 Figure 5.5-6 Pressurizer . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-72 Figure 5.5-7 Reactor Coolant Loop Stop Valve . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-73 Figure 5.5-8 Reactor Vessel Support . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-74 Figure 5.5-9 Steam Generator and Reactor Coolant Pump . . . . . . . . . . . . . . . . . . . 5.5-75

Revision 5209/29/2016 NAPS UFSAR 5-viii Chapter 5: Reactor Coolant System List of Figures (continued)

Figure Title Page Figure 5.5-10 Steam Generator and Reactor Coolant Pump Lower Support . . . . . . . 5.5-76 Figure 5.5-11 Load Paths Into Reinforced Concrete . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-77 Figure 5.5-12 Pressurizer Support . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-78 Figure 5.5-13 Dynamic Model of Steam Generator and Pump Supports . . . . . . . . . . 5.5-80 Figure 5.5-14 Steam Generator-Pump Supports Stress Model. . . . . . . . . . . . . . . . . . 5.5-82 Figure 5.5-15 Dynamic Model for Pressurizer Supports . . . . . . . . . . . . . . . . . . . . . . 5.5-83 Figure 5.5-16 Dynamic Model for Reactor Vessel Supports . . . . . . . . . . . . . . . . . . . 5.5-84 Figure 5.5-17 Temperature Distribution in Snubber Assembly Between Steam Generator Support and Reactor Coolant Pump SupportCase 1, 105°F Ambient . . . . . . . . . . . . . . . . . . . . . . . 5.5-85 Figure 5.5-18 Temperature Distribution in Snubber Assembly Between Steam Generator Support and Reactor Coolant Pump SupportCase 1, 70°F Ambient . . . . . . . . . . . . . . . . . . . . . . . . 5.5-86 Figure 5.5-19 Temperature Distribution in Snubber Assembly Between Steam Generator Support and Concrete WallsCase 2, 105°F Ambient. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5.5-87 Figure 5.6-1 Reactor Coolant System Process Control Instrumentation . . . . . . . . . 5.6-9

Revision 5209/29/2016 NAPS UFSAR 5.1-1 CHAPTER 5 REACTOR COOLANT SYSTEM 5.1

SUMMARY

DESCRIPTION Note: As required by the Renewed Operating Licenses for North Anna Units 1 and 2, issued March 20, 2003, various systems, structures, and components discussed within this chapter are subject to aging management. The programs and activities necessary to manage the aging of these systems, structures, and components are discussed in Chapter 18.

The reactor coolant system, shown in Figure 5.1-1 and Reference Drawings 1 and 2, consists of similar heat transfer loops connected in parallel to the reactor vessel. Each loop contains a reactor coolant pump, a steam generator, and associated piping and valves. In addition, the system includes a pressurizer, a pressurizer relief tank, interconnecting piping and valves, a vent system, and instrumentation necessary for operational control. All the above components are located in the containment building. For arrangement drawings of the reactor coolant system, see Reference Drawings 4 through 10.

During operation, the reactor coolant system transfers the heat generated in the core to the steam generators, where steam is produced to drive the turbine generator. Borated demineralized water is circulated in the reactor coolant system at a flow rate and temperature consistent with achieving the reactor core thermal-hydraulic performance. The water also acts as a neutron moderator and reflector, and as a solvent for the neutron absorber used in chemical shim control.

The reactor coolant system pressure boundary provides a barrier against the release of radioactivity generated within the reactor and is designed to ensure a high degree of integrity throughout the life of the plant.

Reactor coolant system pressure is controlled by the use of the pressurizer, where water and steam are maintained in equilibrium by electrical heaters and water sprays. Steam can be formed (by the heaters) or condensed (by the pressurizer spray) to minimize pressure variations due to the contraction and expansion of the reactor coolant. Spring-loaded safety valves and power-operated relief valves are mounted on the pressurizer and discharge to the pressurizer relief tank, where the steam is condensed and cooled by mixing with water.

The extent of the reactor coolant system pressure boundary is defined as:

1. The reactor vessel, including housing for the control rod drive mechanism.

Revision 5209/29/2016 NAPS UFSAR 5.1-2

2. The reactor coolant side of the steam generators.
3. Reactor coolant pump casing.
4. A pressurizer attached to one of the reactor coolant loops.
5. Pressurizer safety and relief valves.
6. The interconnecting piping, valves, and fittings between the principal components listed above.
7. The pipings, fittings, and valves leading to connecting auxiliary or support systems, up to and including the second isolation valve (from the high-pressure side) on each line.
8. The reactor vessel head vent piping and fittings up to and including the 3/8 inch orifices.

The reactor coolant vent system provides the capability to vent the reactor vessel or the pressurizer using only safety-related equipment.

5.1.1 Reactor Coolant System Components 5.1.1.1 Reactor Vessel The reactor vessel is cylindrical, with a welded hemispherical bottom head and a removable, flanged and gasketed, hemispherical upper head. The vessel contains the core, core-supporting structures, control rods, and other parts directly associated with the core.

The vessel has inlet and outlet nozzles located in a horizontal plane just below the reactor vessel flange but above the top of the core. Coolant enters the vessel through the inlet nozzles and flows down the core barrel-vessel wall annulus, turns at the bottom, and flows up through the core to the outlet nozzles.

5.1.1.2 Steam Generators The steam generators are vertical shell and U-tube evaporators with integral moisture-separating equipment. The reactor coolant flows through the inverted U-tubes, entering and leaving through the nozzles located in the hemispherical bottom head of the steam generator.

Steam is generated on the shell side and flows upward through the moisture separators to the outlet nozzle at the top of the steam generator shell.

5.1.1.3 Reactor Coolant Pumps The reactor coolant pumps are single-speed centrifugal units driven by air-cooled, three-phase induction motors. The shaft is vertical, with the motor mounted above the pumps. A flywheel on the shaft above the motor provides additional inertia to extend pump coastdown. The inlet is at the bottom of the pump; discharge is on the side.

Revision 5209/29/2016 NAPS UFSAR 5.1-3 5.1.1.4 Piping The reactor coolant loop piping is specified in sizes consistent with system requirements.

The hot-leg inside diameter is 29 inches and the cold-leg return line to the reactor vessel is 27.5 inches. The piping between the steam generator and the pump suction is increased to 31 inches in diameter to reduce the pressure drop and improve flow conditions to the pump suction.

5.1.1.5 Pressurizer The pressurizer is a vertical cylindrical vessel with hemispherical top and bottom heads.

Electrical heaters are installed through the bottom head of the vessel, while the spray nozzle and relief and safety valve connections are located in the top head of the vessel.

5.1.1.6 Pressurizer Relief Tank The pressurizer relief tank is a horizontal cylindrical vessel with elliptical ends. Steam from the pressurizer safety and relief valves is discharged into the pressurizer relief tank through a sparger pipe under the water level. This condenses and cools the steam by mixing it with water that is near ambient temperature.

5.1.1.7 Safety and Relief Valves The pressurizer safety valves are of the totally enclosed pop-type. The valves are spring-loaded and self-activated, and they have backpressure compensation. The power-operated relief valves limit system pressure for a large power mismatch and for overpressure protection when NDT protection is required. They are operated automatically or by remote manual control.

Remotely operated valves are provided to isolate the inlet to the power-operated relief valves if excessive leakage occurs.

5.1.1.8 Loop Stop Valves Reactor coolant loop stop valves are remotely controlled, motor-operated gate valves that permit any loop to be isolated from the reactor vessel. One valve is installed on each hot leg and one on each cold leg.

5.1.1.9 Reactor Vessel Head Shielding The reactor vessel head shielding consists of cylindrical steel plate, one inch thick and six feet tall (ASTM A36) which is permanently attached to the intermediate lift ring by special mounting devices. The shielding is comprised of three (3) sections each spanning 120 degrees and weighing 3500 pounds. Cutouts are provided in the shielding for access to the cooling shroud nozzles and the core exit thermocouple nozzle assemblies (CETNAs).

Revision 5209/29/2016 NAPS UFSAR 5.1-4 5.1.2 Reactor Coolant System Performance and Safety Functions The important design and performance characteristics of the reactor coolant system are provided in Table 5.1-1.

5.1.2.1 Reactor Coolant Flow The reactor coolant flow, a major parameter in the design of the system and its components, was established in the original design with a detailed design procedure supported by operating plant performance data, by pump model tests and analyses, and by pressure-drop tests and analyses of the reactor vessel and fuel assemblies. By applying this design procedure described below, it was possible to specify the expected operating flow with reasonable accuracy. This procedure was validated with data from existing operating plants.

With this procedure, three reactor coolant flow rates (best estimate, thermal design, and mechanical design) were identified for the various plant design considerations for the original system design. The definitions of these flows are presented in the following paragraphs, and the application of the definitions is illustrated by the system and pump hydraulic characteristics on Figure 5.1-2.

Two additional reactor coolant flow rates (minimum measured and lower bounding flow) have been identified for specific design considerations. The definitions of these flows are also presented in the following paragraphs.

5.1.2.1.1 Design Flows The best estimate flow is the most likely value for the actual plant operating condition. This flow is based on the best estimate of the reactor vessel, steam generator, and piping flow resistance, and on the best estimate of the reactor coolant pump head flow capacity, with no uncertainties assigned to either the system flow resistance or the pump head. Best estimate flow is used to calculate the core and vessel pressure drops that are listed in Tables 4.4-1 and 4.4-2.

Although the best estimate flow is the most likely value to be expected in operation, more conservative flow rates are applied in the thermal and mechanical designs. The mechanical design of the Robust Fuel Assembly 2 (RFA-2) fuel assemblies has been evaluated at the best estimate flow with uncertainties, which bounds the mechanical design flow.

Thermal design flow is the basis for the reactor core thermal performance (except as noted below), the steam generator thermal performance, and the nominal plant parameters used throughout the design. To provide the required margin, the thermal design flow accounts for the uncertainties in reactor vessel, steam generator, and piping flow resistances; the reactor coolant pump head; and the methods used to measure flow rate. The current thermal design flow is not changed from the original design value.

Revision 5209/29/2016 NAPS UFSAR 5.1-5 Mechanical design flow is the conservatively high flow used in the mechanical design of the reactor vessel internals. To ensure that a conservatively high flow is specified, the mechanical design flow is based on a reduced system resistance and on increased pump head capability. The intersection of this flow resistance with the higher pump curve, as shown on Figure 5.1-2, establishes the mechanical design flow. Pump overspeed due to a turbine-generator overspeed of 20% results in a peak reactor coolant flow of 120% of the mechanical design flow. The overspeed condition is applicable only to operating conditions when the reactor and turbine generator are at power. The current mechanical design flow is not changed from the original design value.

Minimum measured flow is the minimum allowable Reactor Coolant System Total Flow Rate as specified in the North Anna Units 1 and 2 Technical Specifications. This flow rate is less than the best-estimate flow rate and greater than the thermal design flow rate. The minimum measured flow, as stated in Section 5.1.2.2 is used to analyze those events for which the Virginia Power Statistical Evaluation Methodology is the governing departure from nucleate boiling (DNB) methodology. The current minimum measured flow was increased subsequent to steam generator replacement at North Anna.

The lower-bounding design flow is less than the minimum measured flow by an amount which accommodates the uncertainty associated with the methods used to measure, and confirm, the minimum allowable reactor coolant system (RCS) Total Flow Rate. The lower-bounding design flow is greater than the thermal design flow and is used to analyze other departure from nucleate boiling ration (DNBR)-related transients and events which are limited by considerations such as heat sink or pressurization criteria. The lower-bounding design flow was established as a design condition subsequent to steam generator replacement at North Anna.

5.1.2.1.2 Current Thermal Hydraulic Design Flow Conditions Several design changes to the RCS have occurred since the original design was installed at North Anna. These include (a) removal of flow straighteners on intake side of RCP, (b) change in fuel product from 17 x 17 standard fuel (also called LOPAR for LOw PARasitic) to North Anna Improved Fuel (NAIF; see Section 4.2.1), (c) removal of thimble plugging devices (Section 4.4.3.1.1), (d) uprating of the core thermal output to 2893 MWt, (e) replacement of the steam generators, (f) introduction of the Advanced Mark-BW fuel product (see Section 4.5),

(g) uprating of the core thermal output to 2940 MWt, and (h) introduction of the RFA-2 fuel product. Each of these changes had some impact on the RCS flow, however, the replacement of the steam generators had the most discernible impact on the RCS flow rate. The impact was due to the replacement of the original steam generators, which had significant tube plugging, with new steam generators which had increased flow area versus the original steam generators (approximately 6%).

The thermal hydraulic parameter values in Table 5.1-1 are consistent with uprated conditions from the measurement uncertainty recapture power uprate: (a) thermal design flow of

Revision 5209/29/2016 NAPS UFSAR 5.1-6 278,400 gpm; (b) reactor coolant pressure of 2250 psia; (c) reactor power of 2956 MWt; (d) reactor coolant pump net heat of 12 MWt; (e) vessel average temperature of 586.8°F; (f) core bypass of 6.5%; (g) steam pressure of 869 psia with no steam generator tube plugging (851 psia with 7% tube plugging); and (h) feedwater inlet temperature of 449°F. It is noted that the current licensed maximum reactor power is 2940 MWt.

The information presented in this subsection was submitted as part of the original license application with the purpose of supporting operation with an idle loop. This operating condition was not approved by the NRC and has been subsequently prohibited in the North Anna Unit 1 and 2 operating license. Therefore, the information presented in this subsection is maintained for informational purposes only, but does not constitute the current licensing basis of the facilities.

5.1.2.1.3 Flows With One Pump Shut Down The design procedure for calculation of flows with one pump shut down is similar to the procedure described above for calculating flows with all pumps operating. The flows listed in Table 5.1-1 are based on one or both stop valves being closed in the idle loop. For the case where reverse flow exists in the idle loop, the system resistance incorporates the idle loop with a locked rotor pump impeller reverse-flow resistance as a flow path in parallel with the reactor vessel internals. The thermal design flow uncertainty includes a conservative application of parallel flow uncertainties (reactor internals high, idle loop low) as well as the usual component, pump, and flow measurement uncertainties, thereby resulting in a conservatively low reactor flow rate for the thermal design. The mechanical design flow uncertainty is increased slightly to account for the slightly higher uncertainties at the higher pump flows.

5.1.2.2 Interrelated Performance and Safety Functions The interrelated performance and safety functions of the reactor coolant system and its major components are listed below.

1. The reactor coolant system provides sufficient heat transfer capability to transfer the heat produced during power operation and when the reactor is subcritical, including the initial phase of plant cooldown, to the steam and power conversion system.

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2. The system provides sufficient heat transfer capability to transfer the heat produced during the subsequent phase of plant cooldown and cold shutdown to the residual heat removal system.
3. The system heat removal capability under power operation and normal operational transients, including the transition from forced to natural circulation, ensures no fuel damage within the operating bounds permitted by the reactor control and protection systems.
4. The reactor coolant system provides the water used as the core neutron moderator and reflector and as a solvent for chemical shim control.
5. The system maintains the homogeneity of soluble neutron poison concentration and rate of change of coolant temperature such that uncontrolled reactivity changes do not occur.
6. The reactor vessel is an integral part of the reactor coolant system pressure boundary and is capable of accommodating the temperatures and pressures associated with the operational transients. The reactor vessel supports the reactor core and control rod drive mechanisms.
7. The pressurizer maintains the system pressure during operation and limits pressure transients. During a change in plant load, reactor coolant volume changes are accommodated in the pressurizer via the surge line.
8. The reactor coolant pumps supply the coolant flow necessary to remove heat from the reactor core and transfer it to the steam generators.
9. The steam generators provide high-quality steam to the turbine. The tube and tube sheet boundary prevent the transfer of activity generated within the core to the secondary system.
10. The reactor coolant system piping serves as a boundary for containing the coolant under operating temperature and pressure conditions and for limiting leakage (and activity release) to the containment atmosphere. The reactor coolant system piping contains demineralized borated water, which is circulated at the flow rate and temperature consistent with achieving the reactor core thermal and hydraulic performance.

5.1.3 System Operation Brief descriptions of normal anticipated system operations are provided below. These descriptions cover plant start-up, power generation, hot shutdown, cold shutdown, and refueling.

5.1.3.1 Plant Start-up Plant start-up encompasses the operations that bring the reactor plant from cold shutdown to no-load power operating temperature and pressure. A typical plant start-up from cold shutdown is described below.

Before plant start-up, the reactor coolant loops and pressurizer are filled completely, by the use of the charging pumps, with water containing the cold-shutdown concentration of boron. The

Revision 5209/29/2016 NAPS UFSAR 5.1-8 secondary side of the steam generator is filled to normal start-up level with water that meets the steam plant water chemistry requirements.

For refueling, the water level is drained below the reactor vessel flange approximately 4 inches in order to remove the vessel head. Following a refueling, the reactor coolant system must be filled and vented prior to startup.

Gas pockets are vented from the reactor vessel head and the pressurizer by refilling the reactor coolant system. When the filling operation is initiated, the vessel head vent valve is kept open until all gas has been vented, thus venting the vessel head. The pressurizer vent lines are kept open while the pressurizer is filled, thus venting the pressurizer. The steam generator tubes are vented by alternately running the reactor coolant pump in each loop, thus sweeping the gas to the reactor vessel, where it is vented by the head vent.

The reactor coolant system is then pressurized to approximately 300 psig by the use of the low-pressure letdown control valve and the centrifugal charging pumps to obtain the required pressure drop across the seal of the reactor coolant pumps 1-RC-P-1A & -1B; 2-RC-P-1A, 1B, &

1C. The reactor coolant system is then pressurized to approximately 300 psig by the use of the low-pressure letdown control valve and the centrifugal charging pumps to obtain the required pressure drop across the No. 1 seal of the reactor coolant pump 1-RC-P-1C. The pumps may then be operated intermittently to assist in venting operations.

During the operation of the reactor coolant pumps, one charging pump and the letdown path from the residual heat removal loop to the Chemical and Volume Control System are used to maintain the reactor coolant system pressure between 325 and 375 psig. The operation of the reactor coolant pumps 1-RC-P-1A & -1B; 2-RC-P-1A, 1B, & 1C must not be initiated until the pressure differential across the seal is at least 200 psi. The operation of the reactor coolant pump 1-RC-P-1C must not be initiated until the pressure differential across the No. 1 seal is at least 200 psi. For this condition, the system is maintained at approximately 300 psig; the temperature-dependent fracture-prevention pressure limitations of the reactor vessel impose an upper limit on system pressure. The fracture prevention limitations are provided in the Technical Specifications. The charging pump supplies seal injection water for the reactor coolant pump shaft seals. A nitrogen atmosphere and normal operating temperature, pressure, and water level are established in the pressurizer relief tank.

Upon completion of venting, the reactor coolant system is pressurized, all reactor coolant pumps are started, and the pressurizer heaters are energized to begin heating the reactor coolant.

When the pressurizer temperature is approximately 425°F, a steam bubble is formed while the reactor coolant pressure is maintained in the range of 300 to 375 psig. The pressurizer liquid level is reduced until the no-load power-level volume is established. During the initial heatup phase, hydrazine is added to the reactor coolant to scavenge the oxygen in the system; the heatup is not taken beyond 200°F until the oxygen level has been reduced to the specified level.

Revision 5209/29/2016 NAPS UFSAR 5.1-9 The reactor coolant pumps and pressurizer heaters are used to heat the reactor coolant until the minimum temperature for criticality, as defined by the Technical Specifications, is reached.

As the reactor coolant temperature increases, the pressurizer heaters are manually controlled to maintain adequate suction pressure for the reactor coolant pumps. When the normal operating pressure of 2235 psig is reached, pressurizer heater and spray controls are transferred from manual to automatic control.

Refer to Section 5.2.2 regarding protection against the over-pressurization of the reactor coolant system while in a water-solid condition.

5.1.3.2 Power Generation and Hot Shutdown Power generation includes steady-state operation, ramp changes not exceeding the rate of 5% of full power per minute, step changes of 10% of full power (not exceeding full power), and step load changes with steam dump not exceeding the design step load decrease.

During power generation, reactor coolant system pressure is maintained by the pressurizer controller at or near 2235 psig, while the pressurizer liquid level is controlled by the charging-letdown flow control of the Chemical and Volume Control System.

When the reactor power level is less than approximately 15%, the reactor power is controlled manually. At power above approximately 15%, the reactor control system controls automatically maintain an average coolant temperature, consistent with the power relationships, by control rod movement.

During the hot-shutdown operations, when the reactor is subcritical, the reactor coolant system temperature is normally maintained by steam dump to the main condenser. This is accomplished by a controller located in the steam line and operating in the pressure control mode, set to maintain the steam generator steam pressure. Residual heat from the core or operation of a reactor coolant pump provides heat to overcome reactor coolant system heat losses.

5.1.3.3 Plant Shutdown Plant shutdown encompasses the operations that bring the reactor plant from no-load power operating temperature and pressure to cold shutdown. A typical plant shutdown to cold shutdown is described below.

Before plant cooldown, concentrated boric acid solution from the Chemical and Volume Control System is added to the reactor coolant system to increase the reactor coolant boron concentration to that required for cold shutdown. If the reactor coolant system is to be opened during the shutdown, the hydrogen and fission gas in the reactor coolant may be reduced by degassing the coolant in the volume control tank or by using the gas stripper in the boron recovery system.

Revision 5209/29/2016 NAPS UFSAR 5.1-10 Plant shutdown is accomplished in two phases. The first involves the combined use of the reactor coolant system and the steam systems; the second, the residual heat removal system.

During the first phase of shutdown, residual core and reactor coolant heat is transferred to the steam system via the steam generator. Steam from the steam generator is dumped to the main condenser. At least one reactor coolant pump is kept running to ensure uniform reactor coolant system cooldown. The pressurizer heaters are energized and de-energized, and spray flow is manually controlled to cool the pressurizer and depressurize the reactor coolant system while maintaining the required reactor coolant pump suction pressure.

When the reactor coolant temperature is below approximately 350°F and the pressure is in the range of 400 to 450 psig, the second phase of shutdown commences with the operation of the residual heat removal system.

At least one reactor coolant pump is kept running until the coolant temperature is at approximately 160°F. At this temperature, the reactor coolant pump may be turned off.

Pressurizer cooldown can be continued by initiating auxiliary spray flow from the Chemical and Volume Control System. Plant shutdown can continue until the reactor coolant temperature is 140°F or less.

5.1.3.4 Refueling Before removing the reactor vessel head for refueling, the system temperature is reduced to 140°F or less, and hydrogen and fission product levels are reduced. Reactor vessel level during partial drain down is indicated by a local indicator and wide and narrow range indicators on the main control board to determine when the water has been drained below the reactor vessel head vent. Draining continues until the water level is below the reactor vessel flange. The vessel head is then raised as the refueling canal is flooded. Upon completion of refueling, the system is refilled for plant start-up.

5.1.3.5 Loss of Decay Heat Removal Generic Letter 88-17, Loss of Decay Heat Removal, concerns the difficulties and potential consequences involved in preventing, and in recovering from, a loss of cooling to the core while the unit is shut down. (References 1 though 5) The concern resulted in several initiatives to ensure adequate protection from a loss of shutdown cooling, especially during reduced inventory conditions. Reduced inventory is defined to be a reactor coolant system (RCS) level lower than three feet below the reactor vessel flange. This corresponds to an inventory level of 42 inches above centerline of the RCS hot leg piping.

Adequate indication of RCS level and temperature, and of residual heat removal (RHR) system performance, is provided in the control room. A permanent RCS standpipe and an ultrasonic level detector are installed to ensure that at least two independent, continuous RCS level indications are monitored in the control room during reduced inventory conditions. Both

Revision 5209/29/2016 NAPS UFSAR 5.1-11 level monitors provide indication, trending, and low-level alarms in the control room. Whenever the reactor vessel head is located on the reactor vessel, prior to draining the RCS to a reduced inventory condition, at least two core exit thermocouple (CET) temperature indicators are demonstrated to be operable. The CETs continuously indicate in the control room and are periodically recorded on the control room shutdown logs. When the CETs are disconnected due to vessel disassembly, the RHR system temperature indication remains operable and available in the control room. Continuous monitoring of the RHR system performance is provided in the control room by these instruments: suction and discharge temperature indication and trend recording, system flow indication, motor-operated valve (MOV) position indication when energized, pump current indication, pump breaker status indication, system low-flow alarm, pump auto-trip alarm, pump discharge high-pressure alarm, pump cooling water low flow alarm, and component cooling status (e.g. temperature, flow, and pump current).

Controls are in place to implement specific actions to be taken when draining the RCS.

Those actions are based on the Westinghouse Owners Group reduced inventory project guidance and additional plant-specific analyses. The analyses consider the variables affecting time to core boiling, including RCS inventory, RCS temperature, time since shutdown, and total decay heat inventory. The analyses provide the necessary information to determine equipment and operation requirements or limitations, including:

1. Prior to entering a reduced inventory condition, controls are established to provide reasonable assurance containment closure can be achieved prior to the time that core uncovery could result from a loss of decay heat removal. During reduced inventory conditions, at least one boundary on each containment penetration is maintained intact, with the exception of penetrations in use or undergoing maintenance which are under administrative control. In the event of a loss of decay heat removal, a containment closure team is responsible for closing the administratively controlled penetrations.
2. Prior to entering a reduced inventory condition, one charging pump and one low head safety injection pump are maintained available with a specified flowpath to the core.

Administrative controls ensure that additional means of shutdown cooling or inventory make-up are also available.

3. Whenever possible in a reduced inventory condition, activities are avoided that could disrupt stable conditions in the RCS or RHR system, or compensatory actions are taken.

Maintenance activities are assessed prior to implementation for their potential to cause a loss of RCS inventory. Procedures include measures to prevent a loss of RHR and to enhance monitoring for early diagnosis of a loss of RHR.

4. To ensure that pressurization of the reactor vessel upper plenum does not occur upon a loss of cooling, procedures require that the cold leg isolation valve shall be closed first when isolating an RCS loop. When returning an RCS loop to service, the hot leg isolation valve shall be opened first. Whenever maintenance requires an opening on the cold leg during

Revision 5209/29/2016 NAPS UFSAR 5.1-12 reduced inventory operation, procedural controls are in place to ensure a sufficient vent path is available.

These actions are adequate to ensure that decay heat removal capability is maintained.

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5.1 REFERENCES

1. VEPCO Letter Serial No.88-737, Response to Generic Letter 88-17, Loss of Decay Heat Removal, dated January 6, 1989.
2. VEPCO Letter Serial No. 88-737A, Response to Generic Letter 88-17, Loss of Decay Heat Removal, dated February 3, 1989.
3. VEPCO Letter Serial No. 88-737C, Generic Letter 88-17: Loss of Decay Heat Removal Programmed Enhancements for Instrumentation, dated October 3, 1989.
4. VEPCO Letter Serial No. 88-737D, Supplemental Response to Generic Letter 88-17, Loss of Decay Heat Removal, dated November 16, 1990.
5. VEPCO Letter Serial No.91-447, NRC Generic Letter 88-17, Loss of Decay Heat Removal Implementation of Programmed Enhancements, dated November 14, 1991.

5.1 REFERENCE DRAWINGS The list of Station Drawings below is provided for information only. The referenced drawings are not part of the UFSAR. This is not intended to be a complete listing of all Station Drawings referenced from this section of the UFSAR. The contents of Station Drawings are controlled by station procedure.

Drawing Number Description

1. 11715-FM-093A Flow/Valve Operating Numbers Diagram: Reactor Coolant System; Loops 1, 2, & 3; Unit 1 12050-FM-093A Flow/Valve Operating Numbers Diagram: Reactor Coolant System; Loops 1, 2, & 3; Unit 2
2. 11715-FM-093B Flow/Valve Operating Numbers Diagram: Reactor Coolant System, Unit 1 12050-FM-093B Flow/Valve Operating Numbers Diagram: Reactor Coolant System, Unit 2
3. 11715-FM-093E Flow/Valve Operating Numbers Diagram: Reactor Coolant Pump Oil Collection, Unit 1 12050-FM-093E Flow/Valve Operating Numbers Diagram: Reactor Coolant Pump Oil Collection, Unit 2
4. 11715-FM-1A Machine Location: Reactor Containment, Plan, Elevation 291'- 10",

Unit 1 12050-FM-1A Machine Location: Reactor Containment, Plan, Elevation 291'- 10",

Unit 2

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5. 11715-FM-1B Machine Location: Reactor Containment, Plan, Elevation 262'- 10",

Unit 1 12050-FM-1B Machine Location: Reactor Containment, Plan, Elevation 262'- 10",

Unit 2

6. 11715-FM-1C Machine Location: Reactor Containment, Plan, Elevation 241'- 0",

Unit 1 12050-FM-1C Machine Location: Reactor Containment, Plan, Elevation 241'- 0",

Unit 2

7. 11715-FM-1D Machine Location: Reactor Containment, Plan, Elevation 216'- 11",

Unit 1 12050-FM-1D Machine Location: Reactor Containment, Plan, Elevation 216'- 11",

Unit 2

8. 11715-FM-1E Machine Location: Reactor Containment, Sections 1-1 & 5-5, Unit 1 12050-FM-1E Machine Location: Reactor Containment; Sections 1-1, 7-7, 8-8,

& 9-9; Unit 2

9. 11715-FM-1F Machine Location: Reactor Containment; Sections 2-2, 6-6, 7-7, &

10-10; Unit 1 12050-FM-1F Machine Location: Reactor Containment; Sections 2-2, 5-5, & 6-6; Unit 2

10. 11715-FM-1G Machine Location: Reactor Containment, Sections 3-3 & 4-4, Unit 1 12050-FM-1G Machine Location: Reactor Containment, Sections 3-3 & 4-4, Unit 2

Revision 5209/29/2016 NAPS UFSAR 5.1-15 Table 5.1-1 SYSTEM DESIGN AND OPERATING PARAMETERS Plant design life 60 years a Nominal operating pressure 2235 psig Total system volume including pressurizer and surge line 10,000 ft3 (approximately)

System liquid volume, including pressurizer water at 9390 ft3 (approximately) maximum guaranteed power Total nuclear steam supply system heat output at full 10,127 x 106 Btu/hr (2968 MWt) power Total coolant flow rate 104.4 x 106 lb/hr System thermal and hydraulic data Reactor vessel Inlet temperature 551.7°F Outlet temperature 621.9°F P (at T = 551.7°F) 52.6 psid Steam generator Inlet temperature 621.9°F Outlet temperature 551.4°F P (at T = 551.7°F) 34.6 psid Design fouling factor 0.000055 Piping P (at T = 551.7°F) 12.6 psid Reactor coolant pump Inlet temperature 551.4°F Outlet temperature 551.7°F Developed head (at T = 551.7°F) 99.8 psid Developed head 312 ft Flow (each) 92,800 gpm Steam pressure at full power 869 psia (0% SGTP) 851 psia (7% SGTP)

Steam flow at full power (total) 13.20 x 106 lb/hr (0% SGTP) 13.19 x 106 lb/hr (7% SGTP)

Feedwater inlet temperature 449°F Pressurizer spray rate, maximum 880 gpm Pressurizer heater capacity 1400 kW Pressurizer relief tank volume 1300 ft3

a. Original design life was 40 years. The evaluation and management of aging components in this system demonstrate the acceptability of the design life of 60 years.

Revision 5209/29/2016 NAPS UFSAR 5.1-16 Figure 5.1-1 REACTOR COOLANT SYSTEM

Revision 5209/29/2016 NAPS UFSAR 5.1-17 Figure 5.1-2 ORIGINAL DESIGN BASIS PUMP HEAD - FLOW CHARACTERISTICSa

a. The information contained in the figure portrays the original Westinghouse design philosophy with respect to reactor cool-ant system flows. Virginia Power has defined additional reactor coolant flow parameters as described in Section 5.1.2.1.1, Design Flows.

Revision 5209/29/2016 NAPS UFSAR 5.1-18 Intentionally Blank

Revision 5209/29/2016 NAPS UFSAR 5.2-1 5.2 INTEGRITY OF THE REACTOR COOLANT SYSTEM BOUNDARY Reactor coolant system and components are designed and fabricated in accordance with the rules of 10 CFR 50.55a, Codes and Standards, except for certain valves. Based on the projected date of October 1970 for the construction permit, the valves within the reactor coolant system pressure boundary were ordered and supplied in accordance with the requirements of USAS B31.1, 1967, plus addendum, USAS B16.5, and MSS-SP-66. Pressurizer relief valves were ordered and supplied in accordance with USAS B16.5. The original pressurizer safety valves were supplied in accordance with ASME III, 1968 edition. Thus due to the delay in obtaining the actual construction permit until February 1971, the aforementioned valves are not fabricated in accordance with 10 CFR 50.55a. Subsequently, a spare set of valves was procured to ASME III, 2001 edition through 2003 addenda as augmented by 10 CFR 50.55a and Regulatory Guide 1.84. The spare set is used at North Anna Power Station Units 1 and 2 as rotating stock items.

The reactor coolant system boundary is designed to accommodate the system pressures and temperatures attained under all expected modes of plant operation, including all anticipated transients, and to maintain the stresses within applicable stress limits. The system is protected from overpressure by means of pressure-relieving devices, as required by applicable codes.

Materials of construction are specified to minimize corrosion and erosion and to provide a structural system boundary throughout the life of the plant. Fracture prevention measures are taken to prevent brittle fracture. Inspection is in accordance with applicable codes, and provisions are made for the surveillance of critical areas to enable periodic assessments of the boundary integrity.

In accordance with the guidelines of the ASME Code, various ASME-approved Code Cases were used. No specific record of such uses was maintained. The Code Case identified in Table 5.2-1 may have been used for Westinghouse Class 1 components by Westinghouse or by subcontractors or vendors. Table 5.2-2 identifies an ASME Code Case for Class 1 components.

5.2.1 Design Criteria Methods and Procedures 5.2.1.1 Performance Objectives and Design Conditions The performance objectives of the reactor coolant system were described in Section 5.1.

Equipment code and classification lists for the components in the reactor coolant system boundary are in Table 5.2-3.

The reactor coolant system, in conjunction with the reactor control and protection systems, is designed to maintain the reactor coolant at conditions of temperature, pressure, and flow adequate to protect the core from damage. The design requirement for safety is to prevent conditions of high power, high reactor coolant temperature, or low reactor coolant pressure, or combinations of these that could result in a DNB ratio of less than the design DNBR limit.

Revision 5209/29/2016 NAPS UFSAR 5.2-2 The reactor coolant system is designed to provide controlled changes in the boric acid concentration and the reactor coolant temperature. The reactor coolant is the core moderator, reflector, and solvent for the chemical shim. As a result, changes in coolant temperature or boric acid concentration affect the reactivity level in the core.

The following design bases have been selected to ensure that uniform reactor coolant system boron concentration and temperature will be maintained:

1. Coolant flow is provided by either a reactor coolant pump or a residual heat removal pump to ensure uniform mixing whenever the boron concentration is decreased.
2. The design arrangement of the reactor coolant system eliminates dead-ended sections and other areas of low coolant flow in which nonhomogeneities in coolant temperature or boron concentration could develop.
3. The reactor coolant system is designed to operate within the operating parameters, particularly during coolant temperature changes.

The design pressure for the reactor coolant system is 2485 psig, except for the pressurizer relief line from the safety valve to the pressurizer relief tank, which is 600 psig, and the pressurizer relief tank, which is 100 psig. For components with design pressures of 2485 psig, the normal operating pressure is 2235 psig. The design temperature for the reactor coolant system is 650°F, except for the pressurizer and the surge line, which are designed for 680°F, and the pressurizer relief line from the safety valve to the pressurizer relief tank, which is designed for 400°F.

The following five ASME operating conditions are considered in the design of the reactor coolant system:

1. Normal Conditions - Any condition in the course of start-up, operation in the design power range, hot standby, and system shutdown, other than upset, emergency, faulted, or testing conditions.
2. Upset Conditions - Any deviations from normal conditions expected to occur often enough that design should include the ability to withstand the conditions without operational impairment. Upset conditions include those transients that result from any single operator error, control malfunction, transients caused by a fault in a system component requiring its isolation from the system, and transients due to loss of load or power. Upset conditions include any abnormal accidents not resulting in a forced outage and also forced outages for which the corrective action does not include any repair or mechanical damage. The estimated duration of an upset condition is included in the design specifications.
3. Emergency Conditions - Those deviations from normal conditions that require shutdown for the correction of the conditions or repair of system damage. The conditions have a low probability of occurrence but are included to provide assurance that no gross loss of structural integrity will result as a concomitant effect of any damage developed in the system.

Revision 5209/29/2016 NAPS UFSAR 5.2-3 The total number of postulated occurrences for such events shall not cause more than 25 stress cycles having an Sa value greater than that for 106 cycles from the applicable fatigue design curves of the ASME Code,Section III, 1968 Edition.

4. Faulted Conditions - Those combinations of conditions associated with extremely low probability; postulated events whose consequences are such that the integrity and operability of the nuclear energy system may be impaired to the extent that considerations of public health and safety are involved. Such conditions require compliance with safety criteria specified by jurisdictional authorities.
5. Testing Conditions - Testing conditions are those tests in addition to the hydrostatic or pneumatic tests permitted by the ASME Code,Section III, including leak tests or subsequent hydrostatic tests.

To provide the necessary high degree of integrity for the equipment in the reactor coolant system, the transient conditions selected for equipment fatigue evaluation are based on a conservative estimate of the magnitude and frequency of the temperature and pressure transients resulting from various operating conditions in the plant. To a large extent, the specific transient operating conditions to be considered for equipment fatigue analyses are based on engineering judgment and experience. The selected transients are representative of operating conditions that prudently should be considered to occur during plant operation and are sufficiently severe or frequent to be of possible significance to component cyclic behavior. The selected transients may be regarded as a conservative representation of transients that, used as a basis for component fatigue evaluation, provide confidence that the component is appropriate for its application over the design life of the plant.

The following five transients are considered normal conditions:

1. Heatup and Cooldown - For design evaluation, the heatup and cooldown cases are represented by continuous heatup or cooldown at a rate of 100°F/hr for all components in the reactor coolant system except the pressurizer, which is limited to a heatup of 100°F/hr and a cooldown of 200°F/hr. These cases correspond to a heatup or cooldown rate under abnormal or emergency conditions. The heatup occurs from ambient to the no-load temperature and pressure condition; the cooldown represents the reverse situation. In actual practice, the rate of temperature change of 100°F/hr will seldom occur because of other limitations such as the following:
a. Criteria for the prevention of nonductile failure that establish maximum permissible temperature rates of change, as a function of plant pressure and temperature.
b. Slower initial heatup rates when using pumping energy only.
c. Interruptions in the heatup and cooldown cycles attributable to such factors as drawing a pressurizer steam bubble, rod withdrawal, sampling, water chemistry, and gas adjustments.

Revision 5209/29/2016 NAPS UFSAR 5.2-4 The heatup and cooldown rates imposed by plant-operating procedure are limited to 50°F/hr for normal operation. Ideally, heatup and cooldown would occur only before and after refueling. In practice, additional unscheduled plant cooldowns may be necessary for plant maintenance.

2. Unit Loading and Unloading - The unit loading and unloading cases are conservatively represented by a continuous and uniform ramp power change of 5%/min between 15% load and full load. This load swing is the maximum possible consistent with operation with automatic reactor control. The reactor coolant temperature varies with load as prescribed by the temperature control system.
3. Step Increase and Decrease of 10% - The +/-10% step change in load demand is a control transient that is assumed to be a change in turbine control valve opening that might be occasioned by disturbances in the electrical network into which the plant output is tied. The reactor control system is designed to restore plant equilibrium without reactor trip or steam dump following a +/-10% step change in turbine load demand initiated from nuclear plant equilibrium conditions in the range between 15% and 100% full load, the power range for automatic reactor control. In effect, during load-change conditions, the reactor control system attempts to match turbine and reactor outputs such that peak reactor coolant temperature is minimized and reactor coolant temperature is restored to its programmed setpoint at a sufficiently slow rate to prevent excessive pressurizer pressure decrease.

Following a step-load decrease in turbine load, the secondary-side steam pressure and temperature initially increase since the decrease in nuclear power lags behind the step decrease in turbine load. During the same increment of time, the reactor coolant system average temperature and pressurizer pressure also initially increase. Because of the power mismatch between the turbine and reactor and the increase in reactor coolant temperature, the control system automatically inserts the control rods to reduce core power. With the load decrease, the reactor coolant temperature is ultimately reduced from its peak value to a value below its initial equilibrium value at the inception of the transient. The reactor coolant average temperature setpoint change is made as a function of turbine-generator load as determined by first-stage turbine pressure measurement. The pressurizer pressure also decreases from its peak pressure value and follows the reactor coolant decreasing temperature trend. At some point during the decreasing pressure transient, the saturated water in the pressurizer begins to flash, reducing the rate of pressure decrease. Subsequently, the pressurizer heaters come on to restore the plant pressure to its normal value.

Following a step-load increase in turbine load, the reverse situation occurs, that is, the secondary-side steam pressure and temperature initially decrease and the reactor coolant average temperature and pressure initially decrease. The control system automatically withdraws the control rods to increase core power. The decreasing pressure transient is

Revision 5209/29/2016 NAPS UFSAR 5.2-5 reversed by the actuation of the pressurizer heaters and eventually the system pressure is restored to its normal value. The reactor coolant average temperature is raised to a value above its initial equilibrium value at the beginning of the transient.

4. Large-Step Decrease in Load - This transient applies to a step decrease in turbine load from full power of such magnitude that the resultant rapid increase in reactor coolant average temperature and secondary-side steam pressure and temperature automatically initiates a secondary-side steam dump system that prevents a reactor shutdown or lifting of steam generator safety valves. If a steam dump system were not provided to cope with this transient, there would be such a large mismatch between what the turbine is demanding and what the reactor is furnishing that a reactor trip and lifting of steam generator safety valves would occur.

North Anna has been designed for a 50% step change (40% steam dump capability).

However, the transient for a 95% step-load decrease is considered and represents a more severe condition than the lower percentage.

5. Steady-State Fluctuations - The reactor coolant average temperature, for purposes of design, is assumed to increase or decrease a maximum of 6°F in 1 minutes. The temperature changes are assumed to be within +/-3°F of the programmed value of Tavg. The corresponding reactor coolant average pressure is assumed to vary accordingly.

The following five transients are considered upset conditions:

1. Loss of Load Without Immediate Turbine or Reactor Trip - This transient applies to a step decrease in turbine load from full power occasioned by the loss of turbine load without immediately initiating a reactor trip; it represents the most severe transient on the reactor coolant system. The reactor and turbine eventually trip as a consequence of a high-pressurizer-level trip initiated by the reactor trip system. Since redundant means of tripping the reactor are provided as a part of the reactor protection system, transients of this nature are not expected, but are included to ensure a conservative design.
2. Loss of Power - This transient applies to a blackout situation involving the loss of outside electrical power to the station with a reactor and turbine trip. Under these circumstances, the reactor coolant pumps are de-energized, and following the coastdown of the reactor coolant pumps, natural circulation builds up in the system to some equilibrium value. This condition permits the removal of core residual heat through the steam generators, which at this time are receiving feedwater from the auxiliary feed system operating from diesel-generator power.

Steam is removed for reactor cooldown through atmospheric relief valves provided for this purpose.

3. Loss of Flow - This transient applies to a partial loss-of-flow accident from full power in which a reactor coolant pump is tripped out of service as a result of loss of power to the pump. The consequences of such an accident are a reactor and turbine trip on low reactor

Revision 5209/29/2016 NAPS UFSAR 5.2-6 coolant flow, followed by automatic opening of the steam dump system and flow reversal in the affected loop. The flow reversal results in reactor coolant, at cold-leg temperature, being passed through the steam generator and cooled still further. This cooler water then passes through the hot-leg piping and enters the reactor vessel outlet nozzles. The net result of the flow reversal is a sizable reduction in the hot-leg coolant temperature of the affected loop.

4. Reactor Trip from Full Power - A reactor trip from full power may occur for a variety of causes resulting in temperature and pressure transients in the reactor coolant system and in the secondary side of the steam generator. This is the result of continued heat transfer from the reactor coolant in the steam generator. The transient continues until the reactor coolant and steam generator secondary-side temperatures are in equilibrium at zero-power conditions. A continued supply of feedwater and controlled dumping of secondary steam remove the core residual heat and prevent the steam generator safety valves from lifting. The reactor coolant temperature and pressure undergo a rapid decrease from full-power values as the reactor trip system causes the control rods to move into the core.
5. Inadvertent Auxiliary Spray - The inadvertent pressurizer auxiliary spray transient will occur if the auxiliary spray valve is opened inadvertently during normal operation of the plant. This will introduce cold water into the pressurizer with a very sharp pressure decrease as a result.

The temperature of the auxiliary spray water is dependent on the performance of the regenerative heat exchanger. The most conservative case is when the letdown steam is shut off and the charging fluid enters the pressurizer unheated. Therefore, for design purposes, the temperature of the spray water is assumed to be 100°F; the spray flow rate is assumed to be 200 gpm. It is furthermore assumed that the auxiliary spray will, if actuated, continue for 5 minutes until it is shut off.

The pressure decreases rapidly to the low-pressure reactor trip point. At this pressure, the pressurizer low-pressure reactor trip is assumed to be actuated; this accentuates the pressure decrease until the pressure is finally limited to the hot-leg saturation pressure. At 5 minutes the spray is stopped and all the pressurizer heaters return the pressure to 2250 psia. This transient is more severe on a two-loop plant than on a three- or four-loop plant; for example, the pressure decrease is bigger and more rapid. Therefore, the transient for a two-loop plant is used as design basis for all plants.

It is assumed for design purposes that no temperature changes in the reactor coolant system will occur as a result of initiation of auxiliary spray except in the pressurizer.

No transient is classified as an emergency condition.

Revision 5209/29/2016 NAPS UFSAR 5.2-7 The following transients are considered faulted conditions:

1. Reactor Coolant System Boundary Pipe Break - This accident involves the postulated rupture of a pipe in the reactor coolant system boundary. It is conservatively assumed that the system pressure is reduced rapidly and the emergency core cooling system (ECCS) is initiated to introduce water into the reactor coolant system. The safety injection signal also will initiate a turbine and reactor trip.

The criteria for locating design-basis reactor coolant branchline pipe ruptures used in the design of the supports and restraints of the reactor coolant system to ensure continued integrity of vital components and engineered safety systems are given in Section 3.6, and Appendix 3A.

Analyses reported in Reference 1 and service experiences show that the criteria given in Section 3.6 offer a practical equivalent to ensure the same degree of protection to public health and safety as postulating both longitudinal and circumferential breaks at any location in the reactor coolant branchlines. Westinghouse nuclear steam supply system (NSSS) piping and support components are designed to these criteria. Westinghouse performed the stress analysis for the reactor coolant piping and stress analysis for the pressurizer surge line. Stone

& Webster performed the rupture analysis for the surge line and other controlling reactor coolant loop branchlines. Protection criteria against dynamic effects associated with pipe breaks is covered in Section 3.6.

2. Steam-Line Break - For component evaluation, the following conservative conditions are considered:
a. The reactor is initially in hot, zero-power subcritical condition assuming all rods in, except the most reactive rod, which is assumed to be stuck in its fully withdrawn position.
b. A steam-line break occurs inside the containment resulting in a reactor and turbine trip.
c. Subsequent to the break the reactor coolant temperature cools down to 212°F.
d. The ECCS pumps restore the reactor coolant pressure.

The above conditions result in the most severe temperature and pressure variations that the component will encounter during a steam-line break accident.

The dynamic reaction forces associated with circumferential steam-line breaks are considered in the design of supports, restraints, and piping to ensure continued integrity of vital components and engineered safety features.

3. Design-Basis Earthquake - The mechanical stress resulting from the design-basis earthquake is considered on a component basis.

The design conditions are given in the equipment specifications, which are written in accordance with the ASME Code.

Revision 5209/29/2016 NAPS UFSAR 5.2-8 The design transients and the number of cycles of each that is normally used for fatigue evaluations are shown in Table 5.2-4. In accordance with the ASME Code, faulted conditions are not included in fatigue evaluations.

The following tests are carried out before plant start-up:

a. Turbine Roll Test - This transient is imposed on the plant during the hot functional test period for turbine cycle checkout. Reactor coolant pump power is used to heat the reactor coolant to operating temperature, and the steam generated is used to perform a turbine roll test. The plant cooldown during this test may exceed the 100°F/hr maximum rate; however, this test is not detrimental to any plant components.
b. Hydrostatic Test Conditions - The pressure tests are outlined below:
1) Primary-Side Hydrostatic Test Before Initial Start-up - The pressure tests covered by this section include both shop and field hydrostatic tests that occur as a result of component or system testing. This hydro test is performed before initial fuel loading at a water temperature that is compatible with reactor vessel fracture prevention criteria requirements and a maximum test pressure of 3107 psig or 1.25 times the design pressure. In this test, the primary side of the steam generator is pressurized to 3107 psig coincident with no pressurization of the secondary side.
2) Secondary-Side Hydrostatic Test Before Initial Start-up - The secondary side of the steam generator is pressurized to 1.25 times the design pressure of the secondary side coincident with the primary side at 0 psig.
3) Primary-Side Leak Test - Subsequent to each time the primary system has been opened, a leak test is performed. During this test, the primary system pressure is for design analysis purposes, assumed to be raised to 2500 psia, with the system temperature above design transition temperature, while the system is checked for leaks.

In actual practice, the primary system will be pressurized to less than 2500 psia to prevent the pressurizer safety valves from lifting during the leak test.

During this leak test, the secondary side of the steam generator will be pressurized so that the pressure differential across the tubesheet does not exceed 1600 psi. This is accomplished by closing off the steam lines.

Since the tests outlined under items a and b, except b(3), occur before plant start-up, the number of cycles is independent of plant life.

5.2.1.2 Design Evaluation The reactor coolant system provides for heat transfer from the reactor to the steam generators under conditions of forced-circulation flow and natural-circulation flow. The

Revision 5209/29/2016 NAPS UFSAR 5.2-9 heat-transfer capabilities of the reactor coolant system are analyzed in Chapter 15 for various transients.

The heat-transfer capability of the steam generators is sufficient to transfer, to the steam and power conversion system, the heat generated during normal operation, and during the initial phase of plant cooldown under natural-circulation conditions.

The second phase of plant cooldown, cold shutdown, and refueling use the heat exchangers of the residual heat removal system. Their capability is discussed in Section 5.5.4.

The pumps of the reactor coolant system ensure heat transfer by forced-circulation flow.

Design flow rates are discussed in conjunction with the reactor coolant pump description in Section 5.5.1.

Initial reactor coolant system tests were performed to determine the total delivery capability of the reactor coolant pumps. Thus, it was confirmed before initial criticality that adequate circulation is provided by the reactor coolant system.

To ensure a heat sink for the reactor under conditions of natural-circulation flow, the steam generators are at a higher elevation than the reactor. In the design of the steam generators, consideration was given to provide adequate tube area to ensure that the residual heat removal rate is achieved with natural-circulation flow.

To ensure degassification and decay heat removal under certain accident conditions without relying on main coolant pump operation, the reactor coolant vent system provides remote venting capability of the reactor vessel head and pressurizer steam space. Whenever the boron concentration of the reactor coolant system is reduced, plant operation will be such that good mixing is provided to ensure that the boron concentration is maintained uniformly throughout the reactor coolant system.

Although mixing in the pressurizer will not be achieved to the same degree, the fraction of the total reactor coolant system volume that is in the pressurizer is small. Thus, the pressurizer liquid volume is of no concern with respect to its effect on boron concentration.

Also, the design of the reactor coolant system is such that the distribution of flow around the system is not subject to the degree of variation that would be required to produce nonhomogeneities in coolant temperature or boron concentration as a result of areas of low coolant flow rate. An exception to this is the pressurizer, but for the reasons discussed above, it is of no concern. Operation to achieve an orderly shutdown with one reactor coolant pump inoperable is permissible under certain conditions as defined in the Technical Specifications. In this case there would be backflow in the associated loop, even though the pump itself is prevented from rotating backwards by its antirotation device. The backflow through the loop would cause departure from the normal temperatures distribution around the loop, but would maintain the boron concentration in the loop the same as that in the remainder of the reactor coolant system.

Revision 5209/29/2016 NAPS UFSAR 5.2-10 The range of coolant temperature variation during normal operation is limited, and the associated reactivity change is well within the capability of the rod control group movement.

For design evaluation, the heatup and cooldown transients are analyzed by using a rate of temperature change equal to 100°F/hr, which corresponds to abnormal or emergency heatup and cooldown conditions. Over certain temperature ranges, fracture prevention criteria will impose a lower limit to heatup and cooldown rates.

Before plant cooldown is initiated, the boron concentration in the reactor coolant system is increased to the required concentration for the final reactor coolant system temperature, and the concentration is verified by sampling. Thus, during reactor cooldown, no changes are imposed on the boron concentration.

It is therefore concluded that the temperature changes imposed on the reactor coolant system during its normal modes of operation do not cause any abnormal or unacceptable reactivity changes.

The design cycles as discussed in the preceding section are conservatively estimated for equipment design purposes and are not intended to be an accurate representation of actual transients or for all cases to reflect operating experience.

Certain design transients, with associated pressure and temperature curves, have been chosen and assigned an estimated number of design cycles for the purpose of equipment design.

These curves represent an envelope of pressure and temperature transients on the reactor coolant system boundary with margin in the number of design cycles chosen based on operating experience.

To illustrate this approach, the reactor trip transient can be mentioned. Four hundred design cycles are considered in this transient. One cycle of this transient would represent any operational occurrence that would result in a reactor trip. Thus, the reactor trip transient represents an envelope design approach to various operational occurrences. This approach provides a basis for fatigue evaluation to ensure the necessary high degree of integrity for the reactor coolant system components.

System hydraulic and thermal design parameters are used as the basis for the analysis of equipment, coolant piping, and equipment support structures for normal and upset loading conditions. The analysis is performed using a static model to predict deformation and stresses in the system. Results of the analysis give six generalized force components, three bending moments, and three forces. These moments and forces are resolved into stresses in the pipe in accordance with the applicable codes. Stresses in the structural supports are determined by the material and section properties assuming linear elastic small-deformation theory.

In addition to the loads imposed on the system under normal and upset conditions, the design of mechanical equipment and equipment supports requires that abnormal loading conditions such as seismic events and pipe rupture also be considered.

Revision 5209/29/2016 NAPS UFSAR 5.2-11 The analysis of the reactor coolant loops and support systems for seismic loads is based on a three-dimensional, multimass elastic dynamic model. The floor spectral accelerations supplied by VEPCO for North Anna are used as input forcing functions to the detailed dynamic model that includes the effects of the supports and the supported equipment. The loads developed from the dynamic model are incorporated into a detailed loop and support models to determine the support member stresses.

The loop dynamic analysis uses the displacement method, lumped parameter, and stiffness matrix formulations, and assumes that all components behave in a linearly elastic manner. The dynamic analysis of the supports is discussed in Section 5.5.9. Seismic analyses are covered in detail in Section 3.7.

The analysis of the reactor coolant loops and support systems for blowdown loads resulting from postulated breaks on RCL branchlines is based on the time-history response of simultaneously applied blowdown forcing functions on a loop dynamic model.

Since it is highly improbable that maximum load due to postulated pipe ruptures and seismic condition will occur simultaneously, the seismic and pipe rupture loads are combined by the Square Root of Sum of the Squares (SRSS) method. The stresses in the components resulting from normal load directly added to the SRSS of pipe ruptures and seismic loads are determined to verify that the reactor coolant loops and support systems will not loose their function.

For fatigue evaluations, in accordance with the ASME Code, 1968 Edition, maximum stress intensity ranges are derived from combining the normal and upset condition transients given in Section 5.2.1.1. The stress ranges and number of occurrences are then used in conjunction with the fatigue curves in the ASME Code to get the associated cumulative usage factors.

The criterion presented in the ASME Code is used for the fatigue failure analysis. The cumulative usage factor is less than 1.0 and hence the fatigue design is adequate.

The reactor vessel vendors stress report is reviewed by Westinghouse. The stress report includes a summary of the stress analysis for regions of discontinuity analyzed in the vessel, a discussion of the results including a comparison with the corresponding code limits, a statement of the assumptions used in the analyses, descriptions of the methods of analysis and computer programs used, a presentation of the actual calculations used, a listing of the input and output of the computer programs used, and a tabulation of the references cited in the report. The content of the stress report is in accordance with the requirements of the ASME Code.

The Westinghouse analysis of the steam generator tube-tubesheet complex is included as part of the stress report requirement for ASME Code Class A nuclear pressure vessels. The evaluation is based on the stress and fatigue limitations outlined in ASME Code,Section III.

The stress analysis techniques used include all factors considered appropriate to conservative determination of the stress levels used in evaluation of the tube-tubesheet complex.

The analysis of the tube-tubesheet complex includes the effect of all appurtenances attached to the

Revision 5209/29/2016 NAPS UFSAR 5.2-12 perforated region of the tubesheet that are considered appropriate for conservative analysis of the stresses for evaluation on the basis of the ASME Code,Section III, stress limitations. The evaluation involves the heat conduction and stress analysis of the tubesheet, channel head, and secondary-shell structure for particular steady design conditions for which code stress limitations are to be satisfied and for discrete points during transient operation for which the temperature/pressure conditions must be known to evaluate stress maximum and minimum for fatigue life. In addition, analyses are performed to determine tubesheet capability to sustain faulted conditions. The analytic techniques used are computerized.

The major concern in fatigue evaluation of the tube weld is the fatigue strength reduction factor to be assigned to the weld root notch. For this reason, Westinghouse has conducted low-cycle fatigue tests of tube material samples to determine the fatigue strength reduction factor and applied them to the analytic interaction analysis results in accordance with the accepted techniques in the ASME Code for experimental stress analysis. A fatigue strength reduction factor of 4.0 is assigned to the weld root notch in the fatigue evaluation of the tube weld.

The steam generator tube-tubesheet complex integrity is verified by analysis for most adverse conditions resulting from a rupture of either primary or secondary piping.

It has been established that for such accident conditions, where a primary-to-secondary-side differential pressure exists, the primary membrane stresses in the tubesheet ligaments, averaged across the ligament and through the tubesheet thickness, satisfy the conditions given in Tables 5.2-8 and 5.2-11 for this faulted event. Also, for such accident conditions, the primary membrane stress plus primary bending stress in the tubesheet ligaments, averaged across the ligament width at the tubesheet surface location giving maximum stress, must not exceed the faulted condition criteria. In the case of a primary pressure-loss accident, the secondary-primary pressure differential is somewhat higher than the primary-secondary design pressure differential.

However, rigorous analysis shows that no stresses in excess of those covered by the ASME Code for faulted conditions are experienced by the tubesheet for this accident.

Tables 5.2-8 and 5.2-11 summarize the tubesheet stress results for a pressure differential of 2485 psig. Tabulations of other significant results of the tubesheet complex are in Tables 5.2-5 through 5.2-12 and Figure 5.2-1.

The tubes in the North Anna replacement steam generators have been designed to the requirements of the ASME Code, assuming 1600 psi as the design pressure differential. None of the normal and upset conditions impose stresses beyond that normally expected and considered as normal operation by the Code.

A tube analysis for the external pressures showed the collapse pressure of 2389 psi in the straight leg of the tube and 1944 psi in the U-bend region of the tube considering the thinnest tube and including the wear/corrosion allowances for a faulted condition considering the minimum strength properties required by the ASME Code,Section III. This provides a calculated minimum factor of safety of 1.88 against collapse.

Revision 5209/29/2016 NAPS UFSAR 5.2-13 Consideration has been given to the superimposed effects of secondary-side pressure loss and the design-basis earthquake loading. For the case of the tubesheet, the design-basis earthquake loading will contribute an equivalent static pressure loading over the tubesheet of less than 10 psi (for vertical shock). Such an increase is small when compared to the pressure differentials (up to 2485 psig) for which the tubesheet is designed. The fluid dynamic forces under secondary steam break accident conditions indicate, in the most severe case, that the tubes are adequate to constrain the motion of the baffle plates with some plastic deformation, while boundary integrity is maintained.

A complete tube-tubesheet complex analysis verified structural integrity for a primary pressure-loss accident plus the design-basis earthquake.

Although the ASME Code provides for rules and techniques in analysis of perforated plates, it should be noted that the stress intensity levels for perforated plates are given for triangular perforation arrays. Westinghouse tubesheets contain square hole arrays.

Nevertheless, much data have been published that are in excellent agreement with experimental results. The square penetration pattern stress concentration factors and elastic constants that were used in the analysis of the tubesheet were obtained from A Study of Perforated Plates with Square Penetration Patterns (Reference 2). This represented the best available data, which, as the paper demonstrates, has been experimentally justified. The applicable nonmandatory guidelines of Appendix A-8000 were directly used in the analysis in the calculation of the equivalent plate stresses, the use of the stress concentration factors around the pertinent holes, the calculate of the various alternating stresses, and the use of the ASME Code,Section III, fatigue curves.

In the limit stress analysis performed for the tube-tubesheet complex, the deformations and displacements induced at the location of the steam generator supports are negligible. Channel head deflections due to the limit analysis of the tubesheet occur only in the region of the tubesheet and the tubesheet to channel head junction and are not appreciable at the location of the supports.

The support feet are approximately 3 feet away from the tubesheet. Since support deflections due to the tubesheet analysis are negligible, the system analysis will not be affected.

The vessels of the reactor coolant pressure boundary are designated ASME Code,Section III, 1968, including addenda up to Winter 1968, Class A. Piping, pumps, and valves are designated to USAS B31.7, 1969, except as noted in Section 5.2. Additionally, reanalysis of the pressurizer surge line to account for the effect of thermal stratification and striping was performed in accordance with the requirements of ASME Boiler and Pressure Vessel Code,Section III, 1986 and addenda through 1987, incorporating high cycle fatigue as required by NRC Bulletin 88-11.

Loading combination and allowable stresses for ASME Code,Section III, 1968, Winter 1968, Class A components and piping are given in Tables 5.2-13 through 5.2-16. Design criteria for supports are given in Section 5.5.9.

Revision 5209/29/2016 NAPS UFSAR 5.2-14 When the components and systems for the North Anna units were being designed, only general design requirements existed for faulted conditions. There were no specific stress limits or associated methods of analysis established for faulted conditions. To provide a conservative basis for the analysis of Class 1 components, the collapse curves given in the PSAR were developed.

The criteria represented by the collapse curves have evolved into the criteria of Table 5.2-16. The methods and criteria in Table 5.2-16 should thus be reviewed with respect to the criterion agreed to in the PSAR, rather than with the more recently derived methods and limits established in the nonmandatory Appendix F of the ASME Code,Section III. These methods of analysis in conjunction with the faulted condition stress limits ensure that the general design requirements of the NRC for faulted conditions will be met and the plant can thus be safely shut down under accident conditions.

For the reactor coolant loop and components, the elastic system analysis option of Table 5.2-16 was used. Elastic component analyses were used on all components except those discussed below.

Inelastic component analysis was used for the reactor coolant pump support feet. The pump casing with the pump support feet is shown in Figure 5.2-2. The pump foot was analyzed for a set of umbrella loads that are greater than the loads expected in any plant. The umbrella loads are calculated for the faulted condition and each of the maxima of the six load components, Fx, Fy, Fz, Mx, My, Mz, are assumed to occur simultaneously. For example, the maximum Fx is chosen by surveying many past plants, and this is applied simultaneously with the maximum Fy, Fz, Mx, My, Mz, all determined similarly. The actual plant loads are calculated and compared to the umbrella loads. Conformance indicates adequacy of the component for the specific plant application. If conformance is not demonstrated, an individual plant analysis would be performed. Table 5.2-17 indicates the relationship between the North Anna specific plant loads for four different faulted conditions (from four break locations that gave the highest loads) and the umbrella loads for which the pump foot was designed. The actual plant loads are, in themselves, also conservative since the maximum for each of the six load components is determined and assumed to act concurrently with the others. For the loss-of-coolant accident (LOCA) condition, the dynamic time-history analyses show that the maximum values of the six load components do not act concurrently. The seismic event, although evaluated by response spectra analysis, is also dynamic and the load component maxima at the foot clearly will not coincide. Note from Table 5.2-17 that the umbrella loads are greater than these actual plant loads. Note also that the reactor coolant pump support design is such that there are no moments applied to the feet, while the feet are in fact designed to withstand the umbrella moments given in Table 5.2-17. From the preceding discussion, the conservatisms in the actual plant loads and the adequacy of the umbrella loads are therefore demonstrated.

The entire casing foot was analyzed by means of a three-dimensional stress analysis. The foot model used symmetry about the bolt hole radial centerline (Figure 5.2-3). The completed model contains 1584 node points and 1518 three-dimensional solid elements with 4088 active

Revision 5209/29/2016 NAPS UFSAR 5.2-15 degrees of freedom in the model. The three-dimensional finite elements are a mixture of rectangular prisms, triangular prisms, and tetrahedrons. The vertical side and horizontal plate sections have a minimum of four elements through the thickness. The model therefore yields bending stresses as well as direct stresses through the thickness. The higher stress regions have a finer model mesh consisting of smaller tetrahedron and triangular prism elements.

The ANSYS computer code (Reference 3) plastic analysis options were used. The plasticity program is based on incremental strain equations with the Prandtl-Reuss flow rule (Reference 4).

The virgin stress-strain option was used to input the true stress-true strain material curve. To yield the required accuracy, loading increments were computed to keep the size of the plastic strain increments near the size of the material yield strain. The smaller load steps keep the solution process from diverging from the input stress-strain curve.

The resulting faulted condition plastic analysis stress intensity was compared with the faulted condition criteria of 0.7 Sut = 59,950 psi for type 304 stainless steel at 600°F. This is the limit for the primary membrane plus bending stress intensities as given in Table 5.2-16. Since the foot is similar to a beam-type structure, the average stress across the section is very low. The primary bending stresses therefore control. The true ultimate stress, Sut, is determined from the engineering ultimate stress (the engineering stress at the point of maximum load) by assuming constancy of volume. Using this assumption, the true ultimate stress (Sut) is given by:

Sut = Su(1 + e) where e is the engineering strain corresponding to the point of maximum load.

The stresses in the pump foot to casing attachment zone and weld filled region were not controlling. The maximum stress in the foot occurred in the horizontal plate member near the vertical to horizontal plate intersection and in line with the bolt. Since the faulted allowables are based on primary stresses and not peak stresses, the stress components in the high-stress region were linearized through the plate thickness. The resulting maximum stress intensity of the section, found from these linearized maximum principal stresses, was 59,614 psi. This is less than the inelastic allowable.

The maximum located outer fiber strain corresponding to this stress was approximately 12% to 14%. However, the incremental strains for each load step were kept to approximately 0.2%. The maximum deflection calculated by the statically applied loads was approximately 1 in.

at the radial symmetry line passing through the hole. If geometry modifications had been made for this deflection, the load induced in the high-stress regions would have been lowered since the moment arm for the beamline structure would decrease. The present analysis is therefore considered conservative from the analysis as well as the loads standpoint.

The stress and deflection analysis is based on a static application of loads that are physically short-duration, dynamically applied loads. For this reason, the actual deflections due to the short-duration peak loads could be expected to be much lower than those calculated by the static analysis. The actual plant loads are also, in general, considerably lower than the design loads; this

Revision 5209/29/2016 NAPS UFSAR 5.2-16 will further reduce the true magnitude of the deflections. Additional discussion of component supports may be found in Section 5.5.9.

Valves in sample lines are not considered to be part of the reactor coolant system boundary, that is, not ANS Safety Class 1. This is because the nozzles where these lines connect to the reactor coolant system are orificed to a 3/8-inch hole. This hole restricts the flow such that loss through a severance of one of these lines can be made up by normal charging. Pumps and valves are classified as either operating or inactive components for faulted conditions. Operating components are those whose operability is relied on to perform safety function as well as reactor shutdown function during the transients or events considered on the respective operating condition categories. Inactive components are those whose operability (e.g., valve opening or closure, or pump operation or trip) is not relied on to perform the system function during the transients or events considered in the respective operating condition category. The reactor coolant pumps are the only pumps in the reactor coolant system boundary that are classified as inactive for pipe rupture. Table 5.2-18 lists the operating and inactive valves in each line connected to the reactor coolant system up to and including the system boundary. Table 5.2-19 describes the design and operating conditions for active valves in the reactor coolant pressure boundary. Reactor coolant pump overspeed evaluations are covered in Section 5.5.1.3.

Every valve and pump is hydrostatically tested to ASME Code requirements to ensure the integrity of the pressure boundary parts.

5.2.2 Overpressurization Protection 5.2.2.1 Normal Operation The pressurizer is designed to accommodate pressure increases and decreases caused by load transients. The spray system condenses steam to prevent the pressurizer pressure from reaching the setpoint of the power-operated relief valves (PORVs) during a step reduction in power level of 10% of load.

The spray nozzles are located in the top of the pressurizer. Spray is initiated when the pressure exceeds a given setpoint. The spray rate increases proportionally with increasing pressure rate and pressure error until it reaches a maximum value.

The pressurizer is equipped with power-operated relief valves that limit system pressure for a large power mismatch and thus prevent actuation of the fixed high-pressure reactor trip. The relief valves are operated automatically or by remote manual control. The operation of these valves also limits the undesirable opening of the spring-loaded safety valves. Remotely operated stop valves are provided to isolate the power-operated relief valves if excessive leakage occurs.

The relief valves are designed to limit the pressurizer pressure to a value below the high-pressure trip setpoint for all design transients up to and including the design percentage step-load decrease with steam dump but without reactor trip.

Revision 5209/29/2016 NAPS UFSAR 5.2-17 The output signals from the pressurizer pressure protection channels are different from those used for pressure control. The pressure control output signals are used to control pressurizer spray and heaters and power-operated relief valves. Pressurizer pressure is sensed by fast-response pressure transmitters with a time response of better than 0.2 second.

In the event of a complete loss of heat sink, that is, no steam flow to the turbine, protection of the reactor coolant system against overpressure is afforded by pressurizer and steam generator safety valves along with any of the following reactor trip functions:

1. Reactor trip on turbine trip.
2. High pressurizer pressure reactor trip.
3. High pressurizer water level reactor trip.
4. Overtemperature delta T reactor trip.
5. Low-low steam generator water-level reactor trip.

Continued integrity of the reactor coolant system during the maximum transient pressure is ensured by design within the applicable codes as discussed in Reference 5. The Code safety limit is 110% of the 2485 psig design limit.

A detailed functional description of the process equipment associated with the high-pressure trip is provided in Reference 6.

The upper limit of overpressure protection is based on the positive surge of the reactor coolant produced as a result of turbine trip under full load, assuming the core continues to produce full power. The self-actuated safety valves are sized on the basis of steam flow from the pressurizer to accommodate this surge at a setpoint of 2500 psia, an average positive tolerance of

+2% (maximum of +3% per valve), a medium shift of 1%, and a total accumulation of 0.1%. Note that no credit is taken for the relief capability provided by the power-operated relief valves during this surge.

System components whose design pressure and temperature are less than the reactor coolant system design limits are provided with overpressure protection devices and redundant isolation means. System discharge from overpressure protection devices is collected in the pressurizer relief tank in the reactor coolant system.

5.2.2.2 Start-up and Shutdown The plant-specific low temperature overpressure protection system (LTOPS) PORV setpoint analysis was performed to ensure that bounding RCS overpressure protection during start-up and shutdown is provided by the assumed setpoints. The analysis considered the inadvertent start-up of a high-head safety injection pump and the start-up of a reactor coolant pump with a 50°F T between a steam generator and a reactor coolant system cold leg. These two scenarios are the limiting (design basis) mass and energy addition accidents for the development of LTOPS

Revision 5209/29/2016 NAPS UFSAR 5.2-18 setpoints. The isothermal limit curve (i.e., 0°F/hr, or steady state) serves as the design limit for establishing LTOPS setpoints. The validity of this approach is demonstrated by consideration of the conditions at which overpressurization events have been demonstrated to occur and by an analysis which demonstrates margins for this design equivalent to those provided by ASME Section XI Appendix G recommendations for anticipated LTOPS events. This design maximizes the operating margin above the minimum RCS pressure for reactor coolant pump (RCP) operation, thereby minimizing the probability of undesired PORV lifts during RCP start-up.

Above the LTOPS enabling temperature, actuation of the pressurizer safety valves is adequate to ensure reactor vessel integrity during the design basis LTOPS transients. When the RCS is depressurized, an RCS vent path with an opening size equivalent to that of a single pressurizer PORV (i.e., 2.07 in2) is sufficient to prevent RCS overpressurization during the design basis LTOPS transients.

Restrictions on allowable operating conditions and equipment operability requirements have been established to ensure that operating conditions are consistent with the assumptions of the accident analyses. Specifically, RCS pressure and temperature must be maintained within the heatup/cooldown rate-dependent pressure/temperature operating limits specified in the Technical Specifications. Administrative upper limits on heatup rate of 50°F/hr and on cooldown rate of 75°F/hr (Reference 26) are observed. Restrictions on the number of charging pumps capable of inadvertent start-up have been imposed to ensure that the assumptions of the mass addition transient analysis are not invalidated. The LTOPS PORV setpoint analysis imposes no restrictions on the number of low-head safety injection (LHSI) pumps capable of inadvertent injection into the RCS, since the discharge pressure of the LHSI pumps is insufficient to cause the results of the mass addition event analysis to become more limiting. A restriction on the allowable temperature difference between the RCS and steam generator secondary side has been imposed to ensure that the assumptions of the heat addition transient are not invalidated.

The analysis supporting the development of LTOPS setpoints remains valid for cumulative core burnups of 50.3 effective full power year (EFPY) and 52.3 EFPY for North Anna Units 1 and 2, respectively. Bistables are set to preserve the following LTOPS setpoints for these operating periods, and to ensure staggered actuation of PCV-1455C and PCV-1456 (PCV-2455C and PCV-2456 for Unit 2) (Reference 26):

North Anna Unit 1:

PCV-1455C and PCV-1456 540 psig for Cold Leg T 280°F (i.e., 280°F Enabling Temp.)

375 psig for Cold Leg T 180°F North Anna Unit 2:

PCV-2455C and PCV-2456

Revision 5209/29/2016 NAPS UFSAR 5.2-19 540 psig for Cold Leg T 280°F (i.e., 280°F Enabling Temp.)

375 psig for Cold Leg T 180°F Utilizing bistable values lower than those specified increases the margin to the LTOPS design limit heatup and cooldown curve. This provides greater assurance that the design basis LTOPS transients will not result in transient pressures in excess of the design limit. Additional analytical margin is inherent in the assumption that only one PORV is operable, whereas it is highly likely that two PORVs will be available to prevent RCS pressure from exceeding the prescribed limits. The PORVs are described in Section 5.5.8.

The enabling temperature is calculated to conservatively bound the sum of (a) the plant-specific limiting materials RTNDT, (b) margin required by ASME Code Case N-641 (31.9°F), (c) margin for the temperature lag between the quarter-thickness vessel location and the coolant temperature during a 60°F/hr heatup (13°F), and (d) an allowance for temperature measurement instrument uncertainty. Temperature and pressure measurement uncertainties, and the pressure difference between the point of measurement (RCS hot leg) and the point of interest (reactor vessel beltline), were accommodated in the LTOPS setpoint analysis by incorporation of these factors into the design basis (isothermal) pressure/temperature limit curve.

5.2.2.3 Water-Solid Protection The limits for starting a reactor coolant pump while in a water-solid condition are shown in Figure 5.2-4. During solid plant operations, the primary system is filled, the high points are vented, and chemistry is begun to be brought into specifications. The reactor coolant pumps are jogged and the system vented. This is continued until the plant is solid. If the pressurizer chemistry has remained in specification and the loops have not been isolated or drained, a bubble is drawn before starting a reactor coolant pump. To start a reactor coolant pump while the reactor coolant system is in a water-solid condition, the operating procedures require (1) special permission from the operating supervisor and (2) that the associated steam generator secondary-side bulk water temperature is not greater than 50°F above the reactor coolant system temperature. The maximum possible surge rate for this difference in temperature is well within the PORV relief capacity.

The following precautions are also in effect during reactor coolant pump starts. The operating procedures require the residual heat removal system to be in service with the inlet isolation valves open; the low-pressure letdown control valve full open; the normal letdown isolation valves and all three orifice isolation valves open; the reactor coolant system pressure at the lowest allowable pressure for reactor coolant pump operations (300 psig); the charging flow controller at reduced rate; and close operator monitoring of reactor coolant system pressure during venting operations. When reactor coolant system temperature is greater than seal water temperature, permission is required to start a reactor coolant pump.

Revision 5209/29/2016 NAPS UFSAR 5.2-20 The pressure protection systems from the pressure sensors through the PORV solenoids meet both the Seismic Class I and IEEE-279 criteria except Section 4.12 of IEEE-279.

Wide-range hot- to cold-leg temperatures and volume control tank temperature are available to the operator.

The stated administrative controls and the use of redundant dual setpoint relief valves will not require operator action until 10 minutes after a transient is in progress.

5.2.2.4 Pressurized Thermal Shock The Pressurized Thermal Shock (PTS) Rule was approved by the U.S. Nuclear Regulatory Commission on June 20, 1985, and appeared in the Federal Register on July 23, 1985. The PTS Rule outlines regulations to address the potential for PTS events on reactor vessels in nuclear power plants. PTS events are defined as those transients which may result in a rapid and severe cooldown in the primary system, coincident with a high or increasing primary system pressure.

The PTS concern arises if one of these transients acts on the beltline region of a reactor vessel where a reduced fracture resistance exists because of neutron irradiation. Such an event may produce the propagation of flaws postulated to exist near the inner wall surface, thereby potentially affecting the integrity of the vessel.

The code of Federal Regulations (10 CFR 50.61) contains the applicable requirements for calculating the Reference Temperature for Pressurized Thermal Shock (RTPTS) and the associated screening criteria.

Tables 5.2-20 and 5.2-21 provide the results of the 10 CFR 50.61 RTPTS calculations and the NRC screening values for Units 1 and 2, respectively. As these tables demonstrate, all the RTPTS values remain below the NRC screening values for PTS using the projected neutron fluence values through license expiration. This information was provided to the NRC to demonstrate compliance with the PTS rule.

5.2.3 Material Considerations 5.2.3.1 Materials of Construction The materials of construction of the reactor coolant pressure boundary are specified to minimize corrosion and erosion and ensure compatibility with the environment. To minimize internal erosion, the coolant velocity in the piping is limited to about 50 ft/sec.

The reactor vessel closure heads were replaced with closure heads designed for a French nuclear power plant of similar design. The code for the replacement closure head materials was the French R-CCM Code. Equivalence documents were prepared to identify equivalent ASME Code materials. Table 5.2-22 summarizes the materials of construction of the closure heads and provides ASME equivalent materials where appropriate. RCCM/ASME Equivalency ReportBase Material (Reference 20 for Unit 2 and Reference 22 for Unit 1) provide ASME equivalent base materials used for the pressure boundary (including structural attachments).

RCCM/ASME Equivalency ReportFiller Materials (Reference 21 for Unit 2 and Reference 23

Revision 5209/29/2016 NAPS UFSAR 5.2-21 for Unit 1) provide ASME equivalent of the filler materials used for pressure boundary and attachments welded on the closure heads. RCCM/ASME Equivalency ReportsBase Materials and Filler Metals provide analysis and justification for deviations between the codes identified in the base materials and filler materials equivalency reports (References 20, 21, 22, & 23).

5.2.3.1.1 General Material Selection The reactor vessel is constructed of low-alloy steel with 0.125 inch minimum of stainless steel or Inconel weld overlay cladding on all internal surfaces that are in contact with the reactor coolant.

For both units, the reactor vessel beltline shell courses are made of A508 Class 2 forgings.

No additional imposed limits on residual elements were applied to these forgings or the beltline girth weld. Residual elements content is obtained from the excess material from the forging and girth weld that make up the beltline region of the reactor vessel. The chemical analyses that included residual elements will be included in the radiation surveillance reports that were prepared after the first reactor vessel irradiation capsule withdrawal, as discussed in Section 5.4.3.6.

The pressurizer is also constructed of low-alloy steel with austenitic stainless steel weld overlay cladding on all surfaces exposed to the reactor coolant.

All parts of the reactor coolant pump in contact with the reactor coolant are austenitic stainless steel except for seals, bearings, and special parts.

The portions of the steam generator in contact with the reactor coolant water are weld overlay clad with nickel-chromium-iron alloy or austenitic stainless steel. The steam generator tubesheet is weld clad with Inconel; and the heat-transfer tubes are made of Inconel. Table 5.2-22 summarizes the materials of construction of these components.

The reactor coolant piping and fittings that make up the loops are austenitic stainless steel.

All smaller piping that comprises part of the reactor coolant system boundary, such as the pressurizer surge line, spray and relief lines, loop drains, and connecting lines to other systems are also austenitic stainless steel.

All valves in the reactor coolant system that are in contact with the coolant are constructed primarily of stainless steel. Other materials in contact with the coolant, such as materials for hard surfacing and packing, are special materials.

The welding materials used for joining the ferritic-base materials of the reactor coolant boundary conform to or are equivalent to ASME Material Specifications SFA 5.1, 5.2, 5.5, 5.17, 5.18, and 5.20. They are tested and qualified to the requirements of the ASME Code,Section III.

The welding materials used for joining the austenitic stainless steel base materials of the reactor coolant boundary conform to ASME Material Specifications SFA 5.4 and 5.9. They are tested and qualified according to the requirements stipulated in Section 5.2.5.

Revision 5209/29/2016 NAPS UFSAR 5.2-22 The welding materials used for joining nickel-chronium-iron alloy in similar base material combination and in dissimilar ferritic or austenitic base material combination of the reactor coolant boundary conform to ASME Material Specifications SFA 5.11 and 5.14. They are tested and qualified to the requirements of ASME Code,Section III, and are used only in procedures that have been qualified to these same rules.

Instrumentation tubes in the lower vessel head and the control rod drive mechanism (CRDM) nozzles in the upper vessel head are welded with Inconel filler metal after final post-weld heat treatment of the vessel.

The CRDM nozzle to adapter welds were performed by the Continuous Drive Friction process. This process is not permitted by the ASME Code, but is approved by the RCC-M Code and has been used extensively for this application in non-U.S. nuclear plants. The Welding Procedure Specification (WPS), the supporting Procedure Qualification Record (PQR) and Welding Operator Performance Qualification (WPQ) were reconciled to ASME Section IX requirements for the CRDM welds. The destructive tests of the supporting PQR were compared with the required tests and criteria of the ASME Code for an equivalent full penetration weld.

These welds are deemed acceptable for this application at North Anna.

The CRDM vent assemblies (part-length motor tube housings), Type 403 stainless steel, are buttered with Type 309 weld metal, given a post-weld heat treatment, then welded to Type 304 stainless steel, using Type 308 filler metal.

The mechanical properties of representative material heats in the final heat treat condition are determined by test at 650°F design temperature per ASTM E-21 or equivalent. In particular, the hot yield strength (0.2% offset) at 650°F equals or exceeds 19,800 psi.

5.2.3.1.2 Piping Details of the materials of construction and codes used in the manufacture of reactor coolant piping and fittings are given below.

Pipe and fittings are cast, seamless, without longitudinal welds and comply with the requirements of ANSI B31.7 and ASME Code,Section IX.

The minimum wall thicknesses of the pipe and fittings are not less than that calculated using the ANSI B31.7 Class 1 formula of Paragraph I-704.1.2, with an allowable stress value of 17,550 psi allowed for material ASTM A351 Grade CF8A. The minimum bend radius for wrought pipe is 5 nominal pipe diameters.

The pressurizer surge and loop bypass lines conform to ASTM A376 TP 316 with supplementary requirements S2 (transverse tension tests), and S6 (ultrasonic test). The S2 requirements apply to each length of pipe. The S6 requirements apply to 100% of the piping wall volume. The pipe wall thickness for both bypass and pressurizer surge lines is Schedule 160.

Revision 5209/29/2016 NAPS UFSAR 5.2-23 Branch nozzles conform to ASTM A182 Grade F316. Thermal sleeves conform to ASME SA376, Type 316 or SA240, Type 304. The sample scoop conforms to ASTM A182 Grade TP 304 or TP 316. The pressurizer spray scoop conforms to ASTM A403 Grade WP 304 or WP 316.

Stainless steel pipe conforms to ANSI B36.19 for sizes 1/2 inch through 12 inch and schedules 40S through 80S. Stainless steel pipe outside of the scope of ANSI B36.19 conforms to ANSI B36.10, exclusive of the reactor coolant loop piping of special sizes 27-1/2-inch, 29-inch and 31-inch inside diameter.

Flanges conform to ANSI B16.5. Socket weld fittings and joints conform to ANSI B16.11.

The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

5.2.3.1.3 Inspections and Examination Radiographic examination was performed throughout 100% of the wall volume of each pipe and fitting in accordance with the procedure of ASTM E-94 and the acceptance standards of ASTM E-186 Severity Level 2, except that the defect categories D and E were not permissible.

A liquid-penetrant examination was performed on both the entire outside and inside surfaces of each finished fitting in accordance with the procedure of ASME III, 1968, Appendix IX. Acceptance standards were in accordance with Westinghouse NES Equipment Specifications and paragraph N323.4 of the Summer 1969 Addenda to ASME Code,Section III.

All unacceptable defects were eliminated in accordance with the requirements of Westinghouse NES Equipment Specifications.

5.2.3.1.4 Solution Heat Treatment Requirements All of the austenitic stainless steels listed in Tables 5.2-22, 5.2-23, and 5.2-24 were procured from raw material producers in the final heat-treated condition required by the respective ASME Code,Section II, material specification for the particular type or grade of alloy.

5.2.3.1.5 Material Inspection Program All of the wrought austenitic stainless steel alloy raw materials that require corrosion testing after the final mill heat treatment were tested in accordance with ASTM A393 using material test specimens obtained from specimens selected for mechanical testing. The materials were obtained in the solution annealed condition.

5.2.3.1.6 Unstabilized Austenitic Stainless Steels The unstabilized austenitic stainless steels used in the reactor coolant system boundary and components are listed in Table 5.2-22.

Revision 5209/29/2016 NAPS UFSAR 5.2-24 The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

These materials were used in the as-welded condition as discussed in Section 5.2.3.1.4 above. The control of the water chemistry is stipulated in Section 5.2.3.2. These chemistry controls, coupled with the satisfactory experience with components and internals using unstabilized austenitic stainless steel materials that have been post-weld heat treated above 800°F, show acceptability of these heat treatments for stainless steel in PWR chemistry environments (Reference 7). Actual observations of post-weld heat-treated austenitic stainless steels after actual operation indicate no effects of such treatments. Internals heat treated above 800°F from H. B. Robinson Unit 2, Zorita, Connecticut Yankee, San Onofre, Beznau 1, Yankee Rowe, Selni, R. E. Ginna, and SENA have been examined after service and show acceptable material condition.

In all cases where austenitic stainless steel must be given a stress-relieving treatment above 800°F, a high-temperature stabilizing procedure is used. This is performed in the temperature range of 1600 to 1900°F, with holding times sufficient to achieve chromium diffusion to the grain boundary regions based on ASTM A393.

5.2.3.1.7 Avoidance of Sensitization The unstabilized austenitic stainless steels used for core structural load-bearing members and component parts of the reactor coolant pressure boundary were processed and fabricated using the most practicable and conservative methods and techniques to avoid partial or local severe sensitization.

After the material was heat treated, the material was not heated above 800°F during subsequent fabrication except as described in Section 5.2.3.1.9 and the paragraphs below.

Methods and material techniques that were used to avoid partial or local severe sensitization are as follows:

1. Nozzle Safe Ends
a. For the pressurizers, weld deposit with Inconel (Ni-Cr-Fe weld metal F No. 43) was used, followed by the final post-weld heat treatment.
b. For the Unit 1 and Unit 2 replacement steam generators, a SA-336-CLF 316LN forgings welded to Inconel buildup on the nozzle was used.
c. For the reactor vessels, a stainless steel weld metal analysis A-7 containing more than 5% ferrite was used.
2. All welding was conducted using those procedures that have been approved by the ASME Code, Sections III and IX.
3. All welding procedures were qualified by nondestructive and destructive testing according to the ASME Code, Sections III and IX.

Revision 5209/29/2016 NAPS UFSAR 5.2-25 The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

When these welding procedure tests were performed on test welds that were made from base metal and weld metal materials that were from the same lot(s) of materials used in the fabrication of components, additional testing was frequently required to determine the metallurgical, chemical, physical, corrosion, etc., characteristics of the weldment. The additional tests that were conducted on a technical case basis were as follows: light and electron microscopy, elevated temperature mechanical properties, chemical check analysis, fatigue tests, intergranular corrosion tests, and static and dynamic corrosion tests within reactor water chemistry limitations.

4. The following welding methods were tested individually and in multiprocess combinations as outlined above using these prudent energy input ranges for the respective method, as calculated by the following formula:

60EI H = ------------

S where:

H = Joules/in.

E = volts I = amperes S = travel speed in in./min Welding Process Method Energy Input Range, kJ/in Manual shielded tungsten arc 20 to 50 Manual shielded metallic arc 15 to 120 Semiautomatic gas shielded metallic arc 40 to 60 Automatic gas shielded tungsten arc, hot wire 10 to 50 Automatic submerged arc 60 to 140 Automatic electron beam, soft vacuum 10 to 50

5. The interpass temperature of all welding methods was limited to 350°F maximum.
6. All full-penetration welds required inspections in accordance with the codes and rules applicable to each individual component as listed in Table 5.2-3.

5.2.3.1.8 Retesting Unstabilized Austenitic Stainless Steels Exposed to Sensitizing Temperatures In general, it is not feasible to remove samples from fabricated production components to prepare specimens for retest to determine the susceptibility to intergranular attack. These tests were performed only on test welds when meaningful results would predicate production material performance and are as described in Section 5.2.3.1.7 above. No intergranular tests were planned because of satisfactory service experience (see Section 5.2.3.1.6).

Revision 5209/29/2016 NAPS UFSAR 5.2-26 The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

5.2.3.1.9 Compatibility with Reactor Coolant All of the ferritic low-alloy and carbon steels that are used in principal pressure-retaining applications are provided with a 0.125 inch minimum thickness of corrosion-resistant cladding on all surfaces exposed to reactor coolant. This cladding material has a chemical analysis at least equivalent to the corrosion resistance of Types 304 and 316 austenitic stainless steel alloy or nickel-chromium-iron alloy. The other base materials that are used in principal pressure-retaining applications that are exposed to the reactor coolant are austenitic stainless steel, nickel-chromium-iron alloy, and martensitic stainless steel. Ferritic low-alloy and carbon st eel nozzles are safe ended with stainless steel wel d m et al a na l y s i s A - 7 o r nickel-chromium-iron alloy weld metal F No. 43 using weld buttering techniques followed by a post-weld heat treatment. The latter buttering material requires further safe ending with austenitic stainless steel base material after the completion of the post-weld heat treatment when the nozzle is larger than 4-inch nominal inside diameter and/or the wall thickness is greater than 0.531 inch.

The cladding on ferritic-type base materials receives a post-weld heat treatment.

All of the austenitic stainless steel and nickel-chromium-iron alloy base materials are used in the solution anneal heat treated condition. The heat treatments are as required by the material specifications. During subsequent fabrication, these pressure-retaining materials are not heated above 800°F other than instantaneously and locally by welding operations. The solution annealed surge line material is subsequently formed by hot bending followed by a re-solution annealing heat treatment. Corrosion tests are performed in accordance with ASTM A 393.

5.2.3.1.10 Piping Other Than Surge Line and Reactor Coolant Loop Piping This stainless steel piping material purchased for North Anna Power Station conforms to ASTM specifications A312, A358, and A376, which require and define solution annealing parameters to prevent sensitization. Conformance to the applicable ASTM specification for each piece of piping material was certified on mill test reports from the suppliers and is included in the permanent documentation package.

In each case where hot bending was performed on stainless steel piping a furnace chart is provided, documenting the subsequent solution anneal. No hot bending of stainless steel piping was permitted at the construction site.

All welding procedures used in the fabrication and erection of austenitic stainless steel piping systems specify controlled voltage, current, weave parameters, and maximum interpass temperature to limit heat input and sensitization.

5.2.3.1.11 Control of Delta Ferrite on Reactor Coolant Loop and Surge Line Piping

Revision 5209/29/2016 NAPS UFSAR 5.2-27 The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

The austenitic stainless steel welding material used for joining Class I pipe, pump, and fittings is described in Section 5.2.3.1.9 above. The welding material conformed to ASME weld material analysis A-7, Type 308, for all applications. As an option, Type 308L weld filler metal analysis could be substituted for consumable inserts when this technique was used for weld root closures. Bare weld filler metal materials, including consumable inserts used in inert gas welding processes, conformed to ASME SFA-5.9 and were procured to contain not less than 5% delta ferrite. All weld filler metal materials used in flux shielded welding processes conformed to ASME SFA-5.4 or SFA-5.9 and were procured in a wire-flux combination to provide not less than 5% delta ferrite in the deposit.

All welding materials were tested by the fabricator using the specific process(es) and the maximum welding energy inputs to be used in production welding. These tests were in accordance with the requirements of ASME,Section II, material specification, and in addition included delta ferrite determinations. The delta ferrite determinations were made by calculation using the Schaeffler or Modified Schaeffler Constitution Diagram for Stainless Steel Weld Metal.

When subsequent in-process delta ferrite determinations were required and since the welding material conformance was proved by the initial material testing described above, any of the recognized methods for the measurement of delta ferrite were acceptable by mutual agreement. In these instances, sound welds (as determined by visual, penetrant, and volumetric examinations) that display more than 1% average delta ferrite content were considered to be unquestionably acceptable. All other sound welds were also considered acceptable, providing there was no evidence of deviation from qualified procedure parameters or use of malpractices.

If evidence of the latter prevailed, sampling for chemical and metallurgical analysis was required to determine the integrity and acceptability of the weld(s). The sample size was required to be 10% of the welds, but not less than 1 weld, in the particular component or system. If any of these weld samples were defective, that is, failed to pass bend tests as prescribed by ASME Code,Section IX, or the chemical analysis deviated from the material specification, then all remaining welds were sampled and all defective welds were removed and replaced.

All other applications used Type 308 or Type 316, which normally contain 3% to 15%

delta ferrite and 1% to 5% delta ferrite in the deposit analyses, respectively. The successful experience with austenitic stainless steel welds for these applications, supplemented by nondestructive examination, provides assurance for avoiding microfissuring in welds.

The qualification of welding procedures is discussed in Section 5.2.3.1.7 above.

Revision 5209/29/2016 NAPS UFSAR 5.2-28 The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

5.2.3.1.12 Control of Delta Ferrite on All Other Piping Piping systems were fabricated and installed using welding electrodes and consumable inserts purchased to meet the requirements of the applicable sections of ASME Code,Section II. In addition, all electrodes and consumable inserts used in fabrication and erection of austenitic stainless steel systems were purchased with a requirement of 5% to 20% delta ferrite in the undiluted weld metal. The upper limit on delta ferrite need not be applied for welds that do not receive heat treatment subsequent to welding, nor for consumable inserts. The delta ferrite content was checked in two ways: first, by the use of the Schaeffler diagram using actual weld metal chemistry for each heat of material; and second, by Severn gauge measurement of the weld pads prepared in accordance with the applicable part of ASME Code,Section II. All welding procedures specified controlled voltage, current, weave parameters, and maximum interpass temperature to limit heat input.

In addition, 10% of all piping weldments were checked for delta ferrite content. The measurements were performed using a Severn gauge at 90-degree intervals on the weld girth.

Any weldment that exhibited an average as-measured delta ferrite content below 2-1/2% was reported to the engineers. Delta ferrite measurements were recorded on weld data sheets for permanent documentation.

All hard-facing procedures on austenitic stainless steel used low (less than 800°F) preheat temperatures to preclude sensitization of the base metal.

5.2.3.2 Chemistry Control The reactor coolant system chemistry specifications are given in Table 5.2-25.

The reactor coolant system water chemistry is selected to minimize corrosion. Periodic analyses of the coolant chemical composition are performed to verify that the reactor coolant quality meets the specifications.

The Chemical and Volume Control System (CVCS) provides a means for adding chemicals to the reactor coolant system to control the pH of the coolant during initial start-up and subsequent operation, scavenge oxygen from the coolant during startup, and control the oxygen level of the coolant resulting from radiolysis during all power operations. It also provides a means to inject zinc acetate to maintain the zinc concentration while at full power. The oxygen content and pH limits for power operations are shown in Table 5.2-25. A description of the pH control program is found in Section 9.3.4.2.2.1. A description of the zinc program is in Section 9.3.4.2.4.24.

During reactor start-up from the cold condition, hydrazine is used as an oxygen-scavenging agent. The hydrazine solution is introduced into the reactor coolant system in the same manner as for the pH control agent.

Revision 5209/29/2016 NAPS UFSAR 5.2-29 Dissolved hydrogen is used to control and scavenge oxygen produced as a result of the radiolysis of water in the core region. Sufficient partial pressure of hydrogen is maintained in the volume control tank such that the specified equilibrium concentration of hydrogen is maintained in the reactor coolant. A self-contained pressure control valve maintains a minimum pressure in the vapor space of the volume control tank. This can be adjusted to provide the correct equilibrium hydrogen concentration.

Components with stainless steel sensitized in the manner expected during component fabrication and installation will operate satisfactorily under normal plant chemistry conditions in pressurized water reactor systems, because chlorides, fluorides, and particularly oxygen are controlled to very low levels.

5.2.3.3 Fracture Prevention 5.2.3.3.1 Reference Temperature for the Nil-Ductility Transition The reference temperature for the nil-ductility transition (RTNDT) is a calculated parameter which indicates the temperature at which a materials predicted mode of failure transitions from ductile to brittle. RT NDT values are calculated in the manner prescribed by Regulatory Guide 1.99, Revision 2, Radiation Embrittlement of Reactor Vessel Materials. ASME Section XI Appendix G provides guidance for translating the value of RTNDT into a K value, representative of the materials resistance to fracture. Pressure/temperature operating limits are established on the basis of linear-elastic fracture mechanics theory, such that thermal and pressure stresses will not result in combined stresses in excess of the materials resistance to fracture (K). The allowable pressures are revised periodically, often as a result of newly acquired data from the Reactor Vessel Surveillance Program (RVSP) (Section 5.4.3.6). The revised curves are based upon a benchmarked neutron fluence calculation. The use of an RTNDT which includes the projected change in RTNDT due to irradiation provides additional conservatism for the non-irradiated components of the reactor coolant system.

The results of the RVSP are used to verify the predicted shift in RTNDT. Changes in fracture toughness of the core region plates, forgings, weldments, and associated heat-affected zones resulting from radiation damage must be monitored by a surveillance program that conforms with the requirements of ASTM E-185, 1968. (Later editions may be used, but including only those editions through 1982. See References 16 & 27.) The evaluation of the radiation damage in this surveillance program is based on pre-irradiation and post-irradiation testing of Charpy v-notch samples, and tensile specimens carried out during the lifetime of the reactor vessel.

Wedge-opening loading specimens are used in supplemental fracture toughness testing if required. Specimens are irradiated in capsules located near the core mid-height, and are removed from the vessel at specified intervals.

Revision 5209/29/2016 NAPS UFSAR 5.2-30 The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

Pre-irradiation test results for the materials contained in the reactor vessel are given in Tables 5.2-26 (Unit 1) and 5.2-27 (Unit 2). The data presented in these tables were obtained using the actual surveillance report results for both units and the methods described in the Standard Review Plan, Branch Technical Position (BTP) MTEB 5.2. The copper content in both cases was determined using the methods outlined in Reference 8.

The original heatup and cooldown curves were developed before start-up. The predicted shifts in RTNDT values for the original analysis were derived for the quarter-thickness and three-quarter-thickness in the limiting material at 5 EFPY (Unit 1) and 8 EFPY (Unit 2) using the correlated data in Figures 5.2-7 and 5.2-8.

Using the most limiting value of RTNDT for the reactor vessel beltline, steady-state and heatup/cooldown rate-dependent RCS pressure/temperature operating limits are established.

When the Low Temperature Overpressure Protection System (LTOPS) is enabled, the LTOPS setpoints provide bounding protection against exceeding the design basis pressure/temperature limit curve.

The currently applicable heatup and cooldown curves are incorporated in the North Anna Unit 1 and Unit 2 operating license as part of the applicable units Technical Specifications.

Typical heatup and cooldown curves are presented for informational purposes in Figures 5.2-5 and 5.2-6.

The discussion of the Low Temperature Operating Pressure System protection is provided in Section 5.2.2.2.

Temperature and pressure measurement uncertainties, and the pressure difference between the point of measurement (RCS hot leg) and the point of interest (reactor vessel beltline), were accommodated in the pressure/temperature limits analysis by incorporation of these factors into the Technical Specification pressure/temperature limit curves.

The reactor vessel closure heads have been replaced with closure heads that have impact properties exceeding the original head requirements. The low alloy steels have a RTNDT of less than 10°F. The operating stresses in the replacement closure heads are essentially the same as the original heads. Therefore the point of interest (reactor vessel beltline) will not change and the Technical Specification pressure/temperature limit curves will not change as a result of the closure head replacements.

5.2.3.3.2 Thermal Transient Stresses In the event of a large LOCA, the reactor coolant system rapidly depressurizes, and the loss of coolant may empty the reactor vessel. If the reactor is at normal operating conditions before the accident, the reactor vessel temperature is approximately 550°F; if the plant has been in operation

Revision 5209/29/2016 NAPS UFSAR 5.2-31 for some time, part of the reactor vessel is irradiated. At an early stage in the depressurization transient, the emergency core cooling system rapidly injects cold coolant into the reactor vessel.

This results in thermal stress in the vessel wall. To evaluate the effect of the stress, three possible modes of failure are considered: ductile yielding, brittle fracture, and fatigue.

Ductile ModeThe failure criterion used for this evaluation is that there shall be no gross yielding across the vessel wall using the material minimum yield stress specified in Section III of the ASME Code. The combined pressure and thermal stresses during injection through the vessel thickness as a function of time have been calculated and compared to the material yield stress at the times during the safety injection transient.

The results of the analyses showed that local yielding may occur only in approximately the inner 18% of the base metal and in the vessel cladding, complying with the above criterion.

Brittle ModeThe possibility of a brittle fracture of the irradiated core region has been considered using fracture mechanics concepts. This analysis assumes the effects of water temperature, heat-transfer coefficients, and fracture toughness as a function of time, temperature, and irradiation. Both a local crack effect and a continuous crack effect have been considered with the latter requiring the use of a rigorous finite-element axisymmetric computer code. It is concluded on the weight of this evidence that thermal shock resulting from the LOCA will not produce catastrophic failure of the vessel wall even at the end of plant life.

Fatigue ModeThe failure criterion used for the failure analysis was as presented in Section III of the ASME Code (1968). In this method the component is assumed to fail once the combined usage factor at the most critical location for all transients applied to the vessel exceeds the code allowable usage factor of one.

The location in the vessel below the nozzle level that will see the emergency core cooling water and have the highest usage factor will be the incore instrumentation tube attachment welds to the vessel bottom head. As a worst-case assumption, the incore instrumentation tubes and attachment penetration welds are considered to be quenched to the cooling water temperature while the vessel wall maintains its initial temperature before the start of the transient. The maximum possible pressure stress during the transient is also taken into account. This method of analysis is quite conservative and yields calculated stresses greater than would actually be experienced. The resulting usage factor for the instrument tube welds considering all the operating transients and including the safety injection transient occurring at the end of the plant life is below 0.2, which compares favorably with the code allowable usage factor of 1.0.

The generic stress reports for the reactor pressure vessel, steam generator, reactor coolant pump, and pressurizer have been completed, and in all cases the requirements of the applicable ASME Code sections have been satisfied for the design, normal, and upset condition. The faulted condition requirements in Table 5.2-14 are satisfied for the faulted condition loads. The most severely stressed areas can be identified from the stress reports. Even at the most severely stressed areas, all ASME Code requirements are met. The stress reports also include the evaluation of all

Revision 5209/29/2016 NAPS UFSAR 5.2-32 transients required as listed in Section 5.2 and satisfy applicable ASME Code requirements for fatigue evaluation.

It is concluded from the results of these analyses that the delivery of a cold emergency core cooling water to the reactor vessel following a LOCA does not cause any loss of integrity of the vessel.

5.2.3.3.3 Reactor Coolant Pump Flywheel Each reactor coolant pump flywheel consists of two thick plates bolted together. Each plate is fabricated from vacuum degassed A-533 Grade B Class I steel. Supplier certification reports are available for all plate materials providing three Charpy impact energy values at 10°F parallel and normal to the rolling direction.

Determining the acceptability of the flywheel material involves two steps as follows:

1. Establish a reference curve describing the lower bound fracture toughness behavior for the material in question.
2. Use Charpy (CV) impact energy values obtained in certification tests at 10°F to fix position of the heat in question on the reference curve.

A low bound fracture toughness (K Id ) reference curve (see Figure 5.2-9) has been constructed from dynamic fracture toughness data generated by Westinghouse on A-533 Grade B Class I steel (Reference 9). All data points are plotted on the temperature scale relative to the nil-ductility transition temperature (NDTT). The construction of the lower boundary below which no single test point falls, combined with the use of dynamic data when flywheel loading is essentially static, represents a large degree of conservatism.

Of the 12 flywheel plates for North Anna, Units 1 and 2, the lowest Charpy impact energy value measured for any one plate was 32 ft-lb. Corten and Sailors (Reference 10) have determined an empirical formula describing the relationship between KId and CV impact energy at low and intermediate temperatures. Data collected on A-533 Grade B are shown in Figure 5.2-10 with upper and lower scatter bands included. By using this approach and referring to the lower limit of scatter, a fracture toughness (KId) of 46 ksi-in1/2 can be inferred at 10°F corresponding to the CV energy of 32 ft-lb. A considerable degree of conservatism is incorporated into these results. The inferred KId value of 46 ksi-in1/2 is located on the reference curve (Figure 5.2-9) and is assigned at temperature of 10°F. This position is found on the curve at the 18°F position.

A shift to NDTT + 110, which corresponds to the predicted flywheel operating temperature of 120°F, gives a minimum fracture toughness in excess of 100 ksi-in1/2. This conforms to Atomic Energy Commission (AEC) Regulatory Guide 1.14 requirement c that the dynamic stress intensity factor must be at least 100 ksi-in1/2.

By assuming a minimum toughness at operating temperature in excess of 100 ksi-in1/2, it can be seen by examination of the correlation in Figure 5.2-10 that the CV upper-shelf energy

Revision 5209/29/2016 NAPS UFSAR 5.2-33 must be in excess of 50 ft-lb; therefore, the requirement C.l.b. of Regulatory Guide 1.14, that the upper-shelf energy must be at least 50 ft-lb, is satisfied.

It is concluded that flywheel plate materials are suitable for use and meet the Regulatory Guide 1.14 acceptance criteria on the bases of suppliers certification data. Reactor coolant pump flywheel integrity is described in Reference 11.

The calculated stresses at operating speed are based on stresses due to centrifugal forces.

The stress resulting from the interference fit of the flywheel on the shaft is less than 2000 psi at zero speed, but this stress becomes zero at approximately 600 rpm because of radial expansion of the hub.

The primary coolant pumps run at approximately 1190 rpm and may operate briefly at overspeeds up to 109% (1295 rpm) during loss of outside load. However, for conservatism, 125%

of operating speed was selected as the design speed for the primary coolant pumps. The flywheels are given a manufacturers test of 125% of the maximum synchronous speed of the motor.

Precautionary measures, taken to preclude missile formation from primary coolant pump components, ensure that the pumps will not produce missiles under any expected accident condition. Each component of the primary pump motors has been analyzed for missile generation.

Any fragments of the motor rotor would be contained by the heavy stator. The same conclusion applies to the pump impeller because the small fragments that might be ejected would be contained by the heavy casing.

For turbine trips actuated by either the reactor trip system or the turbine protection system, the generator is maintained connected to the external network for 30 seconds to prevent a pump overspeed condition.

5.2.3.4 Cleaning and Contamination Protection It is required that all austenitic stainless steel materials used in the fabrication, installation, and testing of NSSS components and systems be handled, protected, stored, and cleaned according to recognized and accepted methods and techniques. The rules covering these controls are stipulated in the following Westinghouse process specifications. These process specifications supplement the equipment specification and purchase order requirements of every individual austenitic stainless steel component or system that Westinghouse procures for a nuclear steam supply system, regardless of the ASME Code classification. The process specifications are also given to the architect-engineer and to VEPCO for use within their scope of supply and activity.

To ensure that manufacturers and installers adhere to the rules in these specifications, the surveillance of operations by Westinghouse personnel is conducted either in residence at the manufacturers plant and the installers construction site or during periodic engineering and quality assurance visits and audits at these locations.

Revision 5209/29/2016 NAPS UFSAR 5.2-34 The process specifications that establish these rules and that are in compliance with the more current ANSI N45 Committee specifications are as follows:

PS Number 82560HM Requirements for Pressure-Sensitive Tapes for use on Austenitic Stainless Steels.

83336K Requirements for Thermal Insulation Used on Austenitic Stainless Steel Piping and Equipment.

83860LA Requirements for Marking of Reactor Plant Components and Piping.

84350HA Site-Receiving Inspection and Storage Requirements for Systems, Material, and Equipment.

84351NL Determination of Surface Chloride and Fluoride on Austenitic Stainless Steel Materials.

85310QA Packaging and Preparing Nuclear Components for Shipment and Storage.

292722 Cleaning and Packaging Requirements of Equipment for Use in the NSSS.

597756 Pressurized Water Reactor Auxiliary Tanks Cleaning Procedures.

597760 Cleanliness Requirements During Storage Construction, Erection, and Start-up Activities of Nuclear Power Systems.

Controls are imposed during fabrication, construction, and operation to minimize exposure to austenitic stainless steel surfaces to contaminants that could lead to stress corrosion cracking.

Halogen-bearing compounds are avoided or halogen concentration restrictions are observed for shop and field cleaning, packaging, and handling procedures. Precautions are specified for keeping components protected and dry during shipment and storage. Water chemistry controls are required for flushing, testing, and operations to minimize the possibility of stress corrosion cracking. Either stainless steel insulation or nonmetallic insulation with acceptable C1- and (Na+

plus SiO-3), as determined by Figure 1 of Regulatory Guide 1.36 (excluding F- analysis) is used on austenitic stainless steel to minimize the possibility of stress corrosion cracking.

Special cleanliness requirements for NSSS electrical components, instrumentation, core materials, and reactor vessel internals are incorporated into the process specifications.

A specification for site housekeeping based on the ANSI N45 Committee recommendations has also been prepared for North Anna Units 1 and 2. This specification defines area control requirements to ensure that the requisite qualities of each portion of the plant are preserved and that the cleanliness level attained in following the various process specifications is not degraded.

Revision 5209/29/2016 NAPS UFSAR 5.2-35 In general, all of the material listed in Tables 5.2-22 and 5.2-23 that are used in principal pressure-retaining applications and are subject to elevated temperature during system operation are in contact with thermal insulation that covers their outer surfaces.

The thermal insulation used on the reactor coolant boundary is specified to be either reflective stainless steel type or to be made of compounded materials that yield low leachable chloride and/or fluoride concentrations. The compounded materials in the form of blocks, boards, cloths, tapes, adhesives, cements, etc., are silicated to provide the protection of austenitic stainless steels against stress corrosion associated with results from accidental wetting of the insulation by spillage, minor leakage, or other contamination. Each lot of insulation material is qualified and analyzed in accordance with Westinghouse pressurized water reactor (PWR) process specification 83336 KA to ensure that all of the materials provide a compatible combination for the reactor coolant boundary.

The reactor vessel closure head metal reflective insulation used on NAPS Unit 1 and Unit 2 was qualified and analyzed in accordance with Framatome ANP design specifications 08-5023496 and 08-5021646 (References 24 & 25).

In the event of coolant leakage, the ferritic materials will show increased general corrosion rates. Where minor leakage is expected from service experience (valve packing, pump seals, etc.),

materials compatible with the coolant are used. These are shown in Tables 5.2-22 and 5.2-23.

Ferritic materials exposed to coolant leakage can be observed as part of the inservice visual and/or nondestructive inspection program to ensure the integrity of the component for subsequent service.

5.2.4 Reactor Coolant Pressure Boundary Leakage Detection Systems 5.2.4.1 Leakage to the Containment 5.2.4.1.1 Leakage Detection Leakage from the reactor coolant pressure boundary (RCPB) to the containment atmosphere is detected and is indicated in the main control room by one or more of the following methods:

1. Containment gaseous radioactivity monitor (measurement range: 10-106 cpm).
2. Containment particulate radioactivity monitor (measurement range: 10-106 cpm).
3. Containment structure leakage monitoring system.
4. Containment sump monitoring.
5. Reactor coolant system makeup rate.

Indications and alarms are provided for all of the above systems in the control room.

The RCS leakage detection systems monitor and detect leakage from the reactor coolant pressure boundary during normal plant operations and after seismic events to provide prompt and

Revision 5209/29/2016 NAPS UFSAR 5.2-36 quantitative information to the operators to permit immediate corrective actions should the reactor coolant pressure boundary leak be detrimental to the safety of the facility.

These detection systems are generally consistent with the recommendations of Regulatory Guide 1.45, Reactor Coolant Pressure Boundary Leakage Detection Systems, May 1973. The containment atmospheric particulate and gaseous radioactivity monitoring system is not fully seismically qualified. Consistent with Regulatory Guide 1.45 these monitors can perform their intended function during normal plant operations. To ensure the safety function of detecting reactor coolant pressure boundary leakage is maintained after a seismic event the operability of these monitors is required to be verified immediately following a seismic event or the affected unit(s) will be shut down and cooled down to Cold Shutdown.

Generic Letter 84-04, Safety Evaluation of Westinghouse Topical Reports Dealing with Elimination of Postulated Pipe Breaks in PWR Primary Main Loops, dated February 1, 1984 permitted the elimination of the asymmetric blowdown loads resulting for double ended pipe breaks in the main coolant loop piping from the design basis of Westinghouse Owners Group plants with two conditions. The second condition required leakage detection systems at the facility sufficient to provide adequate margin to detect the leakage from a postulated circumferential throughwall flaw utilizing the guidance of Regulatory Guide 1.45 with the exception that seismic qualification of the airborne particulate radiation monitor was not necessary. At least one leakage detection system with a sensitivity capable of detecting 1 gpm in 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> must be operable.

To eliminate the need for a robust support system on the reactor coolant system (RCS) loop bypass lines to protect against the dynamic effect of pipe rupture an augmented inspection program was established and implemented for the RCS bypass lines. In order to support the elimination of augmented inspections on the Reactor Coolant System loop bypass lines, a plant specific Leak-Before-Break (LBB) analysis was performed and submitted to the NRC (Reference 28). This plant specific LBB analysis was approved by the NRC on August 31, 1999 (Reference 29). However, to maintain the same analysis margins required by NUREG-1061 and Draft Standard Review Plan (SRP) Section 3.6.3, Leak-Before-Break Evaluation Procedure, the leakage detection system (radiation monitoring) is required to be capable of detecting a 0.5 gpm leak from the reactor coolant pressure boundary in one hour with an assumed 0.2% failed fuel.

Based on NRCs generic Safety Evaluation Report for Elimination of Postulated Pipe Breaks in PWR Primary Main Loops and the North Anna specific Safety Evaluation Report (amendment numbers 107 for Unit 1 and 93 for Unit 2 dated December 5, 1988), it is no longer necessary to have the containment airborne particulate radiation monitor seismically qualified for the detection of reactor coolant system pressure boundary leakage after a safe shutdown earthquake.

Revision 5209/29/2016 NAPS UFSAR 5.2-37 Following a seismic event, the leakage detection systems will continue to operate with the exception of the containment gaseous and particulate radioactivity monitors and heat load determination from the containment recirculation system coolers.

1. Containment Gas and Particulate Radiation Monitors - Experience has shown that these monitors respond rapidly to reactor coolant system leakage and provide a sensitive indication of such leakage. The time required to detect reactor coolant leakage depends on the size of the break, reactor coolant activity level, and containment background activity.

The sensitivities of the gaseous and particulate monitors are shown in Figure 5.2-11 along with a graph of the time required for the minimum detectable concentration associated with a given leak rate to reach the detector. Both the gaseous radioactivity monitor and the particulate radioactivity monitor have sensitivities such that a 0.5 gpm leak from the reactor coolant pressure boundary can be detected within an hour under the following conditions:

a. There is not prior reactor coolant leakage into the containment.
b. The reactor coolant activities are based on the expected failed fuel values for 0.2% failed fuel.

It has been demonstrated that the radiation monitors have the ability to detect RCS leakage down to 0.5 gpm within one hour threshold range consistent with the assumptions of RG 1.45 for source term (0.2% failed fuel) (Reference 30).

Early in plant life, in conditions of low failed fuel (below 0.01%), the system is not capable of detecting the 0.5 gpm leak within 1 hour1.157407e-5 days <br />2.777778e-4 hours <br />1.653439e-6 weeks <br />3.805e-7 months <br />, as required by the NRC SER (Reference 29).

This inability to meet the sensitivity of the SER holds true for conditions of prior leakage with high-percent failed fuel where existing containment activity could mask any activity increase resulting from a 0.5 gpm increase in leakage.

2. Containment Structure Leakage Monitoring System - Sensitivity of the leakage monitoring system (Section 6.2.7) to leakage from the RCPB is dependent on the sensitivity of the instrumentation.

Instrumentation in the leakage monitoring system that can be used to detect increases in containment temperature and pressure consists of pressure instruments with an uncertainty of 1.055 psi and temperature instruments with an uncertainty of 0.788°F.

The information provided by these instruments can be used to detect increases in containment pressure and temperature that is indicative of a leak from the RCS.

3. Containment Sump - Leakage from unidentified sources will pass to the containment structure in the liquid and vapor phases and will be collected in the containment sump. The containment structure has areas that may temporarily hold up small amounts of liquid and thus prevent the liquid from immediately reaching the containment sump. In addition, the

Revision 5209/29/2016 NAPS UFSAR 5.2-38 containment sump also collects liquid from sources other than the RCPB. The determination of exact RCPB leakage by measuring collected water in the containment sump is not accurate to 1 gpm within 1 hour1.157407e-5 days <br />2.777778e-4 hours <br />1.653439e-6 weeks <br />3.805e-7 months <br /> but is capable of 1 gpm in 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br />.

Leakage from the RCPB by identified sources is collected in portions of the vent and drain system within the containment. These sources include valve packing leakoffs and reactor coolant seal leakoffs. These systems are piped separately and maintained isolated from potential unidentified sources. This system is described in Section 9.3.3.

4. Reactor Coolant System Makeup Rate - Any leakage from the RCPB causes an increase in the amount of makeup water required to maintain normal level in the pressurizer. The demineralized water and concentrated boric acid makeup flow rates are both recorded and alarmed in the main control room.
5. Normal Leakage - Valve stem, seal, and flange systems that are part of the reactor coolant pressure boundary and from which normal design leakage is expected are provided with drains or auxiliary sealing systems. Section 9.3 describes those components from which the leakage is collected either in the primary drain transfer tank or pressurizer relief tank.
a. The reactor coolant pump seal leakoff is described in Section 5.5.1.3.
b. Leakage from the pressurizer safety valves will be identified by temperature sensors that transmit to the main control room. Any temperature increase above the containment ambient temperature that is detected by these sensors will indicate safety valve leakage.
c. Leakage from the reactor vessel flange gasket is piped to the primary drain transfer tank.

Operating experience from the R. E. Ginna plant has indicated that the average total leakage from the reactor coolant system, including the charging and letdown portion of the Chemical and Volume Control System, was about 0.5 gpm. Major sources of this leakage were the reciprocating charging pump seals, averaging about 0.2 gpm, and the valves in the pressurizer spray and spray bypass system, which averaged between 0.2 gpm and 0.5 gpm between repackings.

The North Anna Power Station, Units 1 and 2, uses valves which eliminate the large valve leakages experienced at the R. E. Ginna plant. The pressurizer spray valves are rotary vee ball type control valves, which have less stem leakage than globe type valves, and the pressurizer spray valves bypass valves are weir type diaphragm valves.

Also, the design does not include any reciprocating charging pump (there are three centrifugal charging pumps), so there is no leakage from this source.

Intersystem leakage, such as leakage from the reactor coolant system to the steam generators or from the reactor coolant system to the component cooling system, can be detected by continuous radiation monitors in these two systems. These detection systems are described in Section 11.4.

Revision 5209/29/2016 NAPS UFSAR 5.2-39 While the leakage detection system is not capable of detecting a 1-gpm leak in 1 hour1.157407e-5 days <br />2.777778e-4 hours <br />1.653439e-6 weeks <br />3.805e-7 months <br /> under all conditions, the system is capable of detecting a 5-gpm leak in 1 hour1.157407e-5 days <br />2.777778e-4 hours <br />1.653439e-6 weeks <br />3.805e-7 months <br /> under all conditions. A 1 gpm leak in 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> can also be determined during steady state operation. The identification of leakage sources and the required sensitivity relative to critical cracks are discussed in Section 5.2.4.1.2. Reference 1 discusses critical cracks in piping systems. The results of this report can be used to show that for pipes greater than 4 inches in diameter a crack capable of leaking at 5 gpm is smaller than a critical crack. Therefore, catastrophic failure of the piping system is not expected for this 5-gpm leak. For lines 4 inches and smaller, core cooling analysis shows that breaks of this equivalent cross-sectional area will not result in reactor fuel clad damage; therefore, the sensitivity of 5 gpm under all conditions is justified.

5.2.4.1.2 Identification of Leak Sources Leakage is collected from all components from which significant leakage is expected. Other leakage sources can be roughly located by abnormal changes in temperature or humidity in any specific region of the containment.

Reference 1 shows that, for lines 3 inches or more in diameter, leakage through a critical through-wall crack is considerably greater than the minimum detectable leak.

Reference 1 also provides the length of a critical through-wall crack for lines 2 inches or greater in diameter and the ratio of this crack length to that of a crack permitting 2-gpm leakage for pipe diameters 4 inches and greater. The mathematical model used for this analysis is also given in Reference 1.

5.2.4.1.3 Testing The RCPB leak detection systems are tested periodically as outlined in the Technical Specifications.

5.2.4.1.4 Maximum Allowable Leakage Maximum allowable leakage rates from the RCPB have been established in the Technical Specifications.

5.2.4.2 N-16 Primary to Secondary Leakage Detection System There are four N-16 leak detection systems per unit. Three of the detectors are located adjacent to each of the main steam lines where they enter the Mechanical Equipment Room (MER) and one at the main steam header in the turbine building. They continuously monitor main steam and provide a digital indication and recorder input to the control room. All four N-16 indicators have been located in the existing Westinghouse Radiation Monitoring Cabinets. They provide a digital indication of 1 to 1000 gallons per day of primary to secondary leakage. The recorder display is a 3 decade log scale. Alarm inputs are representative of an alert condition (10 gpd), hi (50 gpd), hi-hi (100 gpd) of leakage above base line data. A system failure alarm also alerts the operator of an internal malfunction. All central processing units (CPUs) are housed in an

Revision 5209/29/2016 NAPS UFSAR 5.2-40 air conditioned N-16 enclosure located in the turbine building on the main operating level, south wall.

The N-16 leak detection systems are designed for continuous operation. Continuous, as used to describe the operation of the N-16 leak detection systems, means that the monitors provide the required information at all times with the following exceptions: (1) the systems are not required to be in operation because of specified plant conditions provided in the Technical Requirements Manual, or (2) a system is out of service for testing or maintenance and approved alternate monitoring methods are in place.

The N-16 leak detection system is an indicating system and does not interact with any plant controlling system. Each steam generator N-16 channel provides an input to the ERF data acquisition system.

5.2.5 Inservice Inspection Programs 5.2.5.1 Program The inservice inspection programs for Units 1 and 2 verify that the structural integrity of the reactor coolant pressure boundary is maintained throughout the life of the station. This verification will ensure compliance with the requirements of 10 CFR 50.55a(g), which requires incorporation of the requirements of Section XI of the ASME Boiler and Pressure Vessel Code, Rules for Inservice Inspection of Nuclear Reactor Coolant Systems.

The ISI programs consist of a preservice or baseline inspection and continuing inspections based on 120-month (10 year) intervals. Each interval requires re-evaluation of the program against the latest Section XI code edition incorporated by reference into 50.55a(g) at the time the program is developed.

Interval and ASME Section XI Code applicability are documented in the ISI Plan. The ISI programs are described in References 12 and 13. These references provide specific information on the scope of the particular units ISI program (including boundaries) and compliance with Section XI (including the applicable code cases incorporated into the ISI program); and they identify those Section XI requirements that are deemed impractical. Relief from these impractical requirements has been developed in accordance with 10 CFR 50.55a(g)(5)(iii).

The following components and areas are available and accessible for visual and nondestructive examination:

1. Reactor vessel: The entire inside surface, including longitudinal and circumferential weld joints.
2. Reactor vessel nozzles: The entire inside surface, including weld joints.
3. Reactor vessel closure head: The entire inside and outside surfaces, including weld joints.
4. Reactor vessel studs, nuts, and washers.

Revision 5209/29/2016 NAPS UFSAR 5.2-41

5. Welds between the main coolant piping, reactor vessel, steam generators, reactor coolant pumps, the chemical and volume control piping, and safety injection system piping.
6. Reactor internals and supports.
7. Reactor vessel flange seal surface.
8. CRD shafts.
9. CRDM assemblies.
10. Selected areas of reactor coolant pipe external surfaces (except for the 5-foot penetration of the primary shield).
11. Steam generator: The external surface, the internal surfaces of the steam drum, and the channel head.
12. Pressurizer: The internal and external surfaces.
13. Reactor coolant pump: The external surfaces, motor, and impeller.
14. Loop stop valves.
15. Regenerative heat exchanger: The external surface and nozzle welds.

A discussion of exceptions to the ASME Code,Section XI, including justifications for those exceptions, was submitted to the NRC (References 14 & 15).

The considerations that are incorporated into the reactor coolant system design to permit the above inspections are the following:

1. All reactor internals are completely removable. The storage space required to permit these inspections is provided.
2. The closure head is stored dry in the containment structure during refueling to facilitate direct visual inspection.
3. All reactor vessel studs, nuts, and washers are removed to dry storage during refueling.
4. Provision is made to remove portions of the supplementary neutron shield of the coolant nozzles. The insulation covering the nozzle welds may be removed.
5. Access holes in the lower internals barrel flange allow remote access to the reactor vessel internal surfaces between the flange and the nozzles without the removal of the internals.
6. A removable plug in the lower core support plate allows access for the inspection of the bottom head without removal of the lower internals.
7. The storage stands for the storage of the upper internals package allow inspection access to both the inside and outside of the structure. No permanent storage stand is provided for the lower internals package. However, it can be removed from the reactor vessel and temporarily stored.

Revision 5209/29/2016 NAPS UFSAR 5.2-42

8. The CRDM design allows the removal of the mechanism assembly from the reactor vessel head by the cutting of seal welds.
9. Manways are provided in the steam generator steam drum and channel head to allow access for internal inspection.
10. A manway is provided in the pressurizer top head to allow access for internal inspection.
11. Insulation on primary system components (except the reactor vessel) and selected portions of the piping (except for the penetration in the primary shield) may be removed.

Conventional nondestructive test techniques can be used for the inspection of primary loop components other than the reactor vessel. The reactor vessel presents special problems because of radiation levels and underwater accessibility that restrict usual test techniques. The following steps are incorporated in the design, manufacturing, and installation to prepare the vessel for nondestructive examinations:

1. Shop ultrasonic examinations were performed on all internally clad surfaces to an acceptance and repair standard to ensure an adequate cladding bond to allow later ultrasonic testing of the base metal from the inside surface. The size of cladding bond defect allowed was 1/4 inch by 3/4 inch with the greater direction parallel to the weld.
2. Ultrasonic examinations and mapping of all pressure boundary welds on the vessel were performed after installation to provide a baseline for future ultrasonic examinations.
3. The internal reactor vessel shell, in the core area, presents a clean, uncluttered cylindrical surface that permits the positioning of test equipment without obstruction.
4. During the manufacturing stage, additional areas of the reactor vessel were tested by ultrasonic methods and mapped to provide further assurance that any indications were below acceptance thresholds.

It is planned to use automated, remote ultrasonic examination techniques to volumetrically examine pressure boundary welds in the reactor vessels. The internal surface of the reactor vessels will be inspected periodically using optical devices over the accessible areas. During refueling, the vessel cladding will be inspected in certain areas between the closure flange and the primary coolant inlet nozzles, and, if deemed necessary by this inspection, the core barrel will be removed making the entire inside vessel surface accessible. Externally, the CRDM nozzles on the closure head, the instrument nozzles on the bottom of the vessel, and the extension spool pieces on the primary coolant outlet nozzles are accessible for inspection during refuelings.

The closure head is examined visually during each refueling. Optical devices permit visual inspection of the cladding. CRDM nozzles on the closure head, the instrument nozzles on the bottom of the vessel, and the extension spool pieces on the primary coolant nozzles are accessible for inspection during refuelings.

Revision 5209/29/2016 NAPS UFSAR 5.2-43 Records are maintained in accordance with Section IS-600 of the edition of the ASME Code and addenda to which the inservice inspection is being conducted.

Additional augmented inservice inspection programs for high-energy piping within the containment and outside the containment are discussed in Section 3.6.

5.2.5.2 Inservice Inspection Equipment The equipment planned for use in performing the reactor vessel and nozzle baseline and inservice inspections consists of a remote-controlled manipulator mounted internally in the vessel, which will automatically position ultrasonic transducers to carry out the prescribed examinations.

The baseline data enables the reinstallation of the automated inspection machine during the inservice inspections phase to duplicate the original machine and transducer settings. In this manner, changes from the original examinations can be detected. In addition to CRT displays, hand copy printed tapes will be provided.

5.2.5.3 Loose Parts Monitoring The loose parts monitoring system for each unit consists of 10 sensors and appropriate signal conditioners that monitor vibration and impacts from slightly below audible (about 20 Hz) to near the top end of audible (about 15kHz). Of these 10 sensors, 5 are active, with circuitry that is complete; the remaining 5 are reserve or standby units with sensors in place and cabling and preamplifiers installed. Toggle switches connect either the active or passive sensors into the active channel.

An active sensor and a reserve sensor are located at each of the following positions:

1. Reactor vessel head flange.
2. Reactor vessel bottom (instrument tube).
3. Steam generators A, B, and C above tubesheet.

Signal preamplifiers and shielded cable are used to transmit the signals to the control room.

Signal readout in the control room consists of the following:

1. Visual displays.
a. A digital meter with a selector switch to monitor the level of the wideband signal of each channel. Each noise bi-stable module will have a light to indicate vibration and loose parts conditions.
b. A three-pen chart recorder provides for real-time data analysis.
2. Audio monitoring of any channel by a speaker and headphones. A switch is provided for selecting the output from any single channel.

Revision 5209/29/2016 NAPS UFSAR 5.2-44

3. Auxiliary outputs provided for both active and passive channels allow monitoring with external equipment such as oscilloscopes, oscillographs, and spectrum analyzers.

5.2.5.4 Vibration Monitoring The vibration monitoring system is an adaptation of the Bently Nevada Series 3500 monitoring system for use on the Westinghouse reactor coolant pumps to provide continuous monitoring of both shaft and frame vibration.

The following equipment is supplied on each unit:

1. Proximeter probes (three per pump) measure shaft vibration in the horizontal and vertical directions (one probe in each direction). The third probe is known as the keyphasor probe, and provides a timing measurement of the rotating shaft, to aid in balancing.
2. Velocity probes (two per pump) measure frame vibration, mounted at the top of the motor support stand.
3. Proximeters (three per pump) - amplifying units that condition the electrical energy supplied to the probe and adjust the signal returned from the probe to provide a voltage output proportional to distance change.
4. Vibration amplitudes are displayed on a recorder (one per unit).
5. Keyphasor modules (two per unit) provide plug jacks for the readout of the keyphase probe balancing.
6. Dual power supply modules provide operating voltages for all probes and transducers.

Items 1 through 3 are located inside the containment and mounted on the pump and motor support stand.

Revision 5209/29/2016 NAPS UFSAR 5.2-45

5.2 REFERENCES

1. J. J. Szyslowski and R. Salvatori, Determination of Design Pipe Breaks for the Westinghouse Reactor Coolant System, WCAP-7503, Revision 1, 1972.
2. W. J. ODonnell, A Study of Perforated Plates with Square Penetration Patterns, WRC 124, 1967.
3. G. J. DeSalvo and J. A. Swanson, ANSYS Users Manual, Engineering Analysis Systems Report, 1972.
4. A. Mendleson, Plasticity: Theory and Application, MacMillan, New York, 1968.
5. K. Cooper, R. M. Starek, and V. Miselis, Overpressure Protection for Westinghouse Pressurized Water Reactors, WCAP-7769, Revision 1, 1972.
6. J. A. Nay, Process Instrumentation for Westinghouse Nuclear Steam Supply Systems, WCAP-7671, 1971.
7. W. S. Hazelton, Sensitized Stainless Steel in W PWR Nuclear Steam Supply System, WCAP-7735, 1971.
8. W. W. Hazelton et al., Basis for Heatup and Cooldown Limit Curves, WCAP-7924, 1972.
9. W. O. Shabbits, Dynamic Fracture Toughness Properties of Heavy Section A-533 Grade B Class 1 Steel Plate, WCAP-7623, 1970.
10. H. T. Corten and R. H. Sailors, Relationship Between Material Fracture Toughness Using Fracture Mechanics and Transition Temperature Tests, UILU-ENG 71-600, 1971.
11. R. Salvatori, Reactor Coolant Pump Integrity in LOCA, WCAP-8163, Westinghouse Electric Corporation, 1973.
12. Inservice Inspection Program for Components and Component SupportsUnit 1.
13. Inservice Inspection Program for Components and Component SupportsUnit 2.
14. VEPCO letter 480/101977 to E. G. Case, NRC, dated December 16, 1977.
15. VEPCO letter dated May 22, 1987 (Serial #86-796A).
16. Letter from USNRC to J. P. OHanlon, North Anna Power Station Unit 1 and Unit 2Revision to Reactor Vessel Surveillance Capsule Withdrawal Schedule, Serial No.99-446, dated August 13, 1999.
17. Letter from L. N. Hartz to USNRC, Virginia Electric and Power Company, North Anna Power Station Units 1 and 2, Surry Power Station Units 1 and 2, Evaluation of Reactor Vessel Materials Surveillance Data, Serial No. 99-452A, dated November 19, 1999.
18. Letter from L. N. Hartz to USNRC, Virginia Electric and Power Company, North Anna Power Station Unit 2, Evaluation of Reactor Vessel Materials Surveillance Data, Serial No.00-463, dated September 19, 2000.

Revision 5209/29/2016 NAPS UFSAR 5.2-46

19. Letter from L. N. Hartz to USNRC, Virginia Electric and Power Company, North Anna Power Station Unit 2, Application of Sequoyah 2 Surveillance Data to North Anna Unit 2 Reactor Vessel Weld Material Fabricated from Weld Wire Heat 4278, Serial No.01-262, dated April 27, 2001.
20. Framatome ANP Document No. 38-1290372, RCCM/ASME Equivalency ReportBase Materials for North Anna Unit 2 Reactor Vessel Closure Head.
21. Framatome ANP Document No. 38-1290373, RCCM/ASME Equivalency ReportFiller Materials for North Anna Unit 2 Reactor Vessel Closure Head.
22. Framatome ANP Document No. 38-1290441, RCCM/ASME Equivalency ReportBase Materials for North Anna Unit 1 Reactor Vessel Closure Head.
23. Framatome ANP Document No. 38-1290448, RCCM/ASME Equivalency ReportFiller Materials for North Anna Unit 1 Reactor Vessel Closure Head.
24. Framatome ANP Document 08-5021646, Replacement RVCH Insulation North Anna 2, Revision 01, December 2002.
25. Framatome ANP Document 08-5023496, Replacement RVCH Insulation North Anna 1, Revision 00, February 2003.
26. Letter from W.R. Matthews to USNRC, Virginia Electric and Power Company, North Anna Power Station Units 1 and 2, Proposed Technical Specifications Change Request, Reactor Coolant System Pressure/Temperature Limits, LTOPS Setpoints and LTOPS Enable Temperatures, Serial No.04-380, dated July 1, 2004.
27. Letter from USNRC to D.A. Christian, North Anna Power Station, Unit Nos. 1 and 2 (North Anna 1 and 2)Approval of Proposed Reactor Vessel Material Surveillance Capsule Withdrawal Schedule (TAC Nos. MC6412 and MC6413), Serial No.06-271, dated March 15, 2006.
28. Letter from J. P. OHanlon, Virginia Electric and Power Company, North Anna Power Station Units 1 and 2, Protection Against Dynamic Effects Associated with a Loss of Coolant Accident, dated June 23, 1998, Serial No.98-013.
29. Letter from USNRC to J. P. OHanlon, North Anna Power Station, Unit 1 and Unit 2, Protection Against Dynamic Effects Associated with a Loss-of-Coolant Accident (TAC Nos.

MA2301 and MA2302), dated August 31, 1999.

30. Letter from D. A. Christian, Virginia Electric and Power Company, North Anna Power Station Units 1 and 2, Request for Additional Information, Leak Detection System Sensitivity for Leak-Before-Break Application on Reactor Coolant Loop Bypass Lines, dated July 9, 1999, Serial No.99-331.

Revision 5209/29/2016 NAPS UFSAR 5.2-47 Table 5.2-1 ASME CODE CASES FOR WESTINGHOUSE PWR CLASS 1 COMPONENTS Code Case Title 1141 Foreign Produced Steel 1332 Requirements for Steel Forgings 1334 Requirements for Corrosion Resistant Steel Bars 1335 Requirements for Bolting Material 1337 Requirements for Special Type 403 Modified Forgings or Bars (Section III) 1344 Requirements for Nickel-Chromium Age-Hardenable Alloys 1345 Requirements for Nickel-Molybdenum-Chromium-Iron Alloys 1355 Electroslag Welding 1358 High Yield Strength Steel for Section III Construction 1360 Explosive Welding 1361 Socket Welds 1364 Ultrasonic Transducers SA-435 (Section II) 1384 Requirements for Precipitation Hardening Alloy Bars and Forgings 1388 Requirements for Stainless Steel - Precipitation Hardening 1390 Requirements for Nickel-Chromium Age-Hardenable Alloys for Bolting 1395 SA-508, Class 2 Forgings - Modified Manganese Content 1401 Welding Repair to Cladding 1407 Time of Examination 1412 Modified High Yield Strength Steel 1414 High Yield Strength Cr-Mo 1423 Plate; Wrought Type 304 and 316 with Nitrogen Added 1433 Forgings; SA-387 1434 Class 8N Steel Casting (Postweld Heat Treatment for SA-487) 1448 Use of Case Interpretations of ANSI B31 Code for Pressure Piping 1456 Substitution of Ultrasonic Examination 1459 Welding Repairs to Base Metal 1461 Electron Beam Welding 1470 External Pressure Charts for Low Alloy Steel

Revision 5209/29/2016 NAPS UFSAR 5.2-48 Table 5.2-1 (continued)

ASME CODE CASES FOR WESTINGHOUSE PWR CLASS 1 COMPONENTS Code Case Title 1471 Vacuum Electron Beam Welding of Tube Sheet Joints 1474 Integrally Finned Tubes (Section III) 1477 B31.7, ANSI 1970 Addenda 1484 SB-163 Nickel-Chromium-Iron Tubing at a Specified Minimum Yield Strength of 40,000 psi 1487 Evaluation of Nuclear Piping for Faulted Conditions 1492 Postweld Heat Treatment 1493 Postweld Heat Treatment 1494 Weld Procedure Qualification Test 1495 Stress Indices in Table NB-3683.2-1 1498 SA-508, Class 2, Minimum Tempering Temperature 1501 Use of SA-453 Bolts in Service Below 800°F without Stress Rupture Tests 1504 Electrical and Mechanical Penetration Assemblies 1505 Use of 26 Cr-1 Mo Steel 1508 Allowable Stresses, Design Stress Intensity and/or Yield Strength Valves 1514 Fracture Toughness Requirements 1515 Ultrasonic Examination of Ring Forgings for Shell Section of Section III, Class 1 Vessels 1516 Welding of Non-Integral Seats in Valves for Section III Application 1517 Material Used in Pipe Fittings 1519 Use of A-105-71 in lieu of SA-105 1521 Use of H. Grades SA-240, SA-479, SA-336, and SA-358 1522 ASTM Material Specifications 1523 Plate Steel Refined by Electroslag Remelting 1524 Piping 2 in. NPS and Smaller 1525 Pipe Descaled by Other Than Pickling 1526 Elimination of Surface Defects 1527 Integrally Finned Tubes 1528 High Strength SA-508 Class 2 and SA-541 Class 2 Forgings for Section III Construction of Class 1 Components

Revision 5209/29/2016 NAPS UFSAR 5.2-49 Table 5.2-1 (continued)

ASME CODE CASES FOR WESTINGHOUSE PWR CLASS 1 COMPONENTS Code Case Title 1529 Material for Instrument Line Fittings 1531 Electrical Penetrations, Special Alloys for Electrical Penetrations Seals 1534 Overpressurization of Valves 1535 Hydrostatic Test of Class 1, Nuclear Valves 1539 Metal Bellows and Metal Diaphragm Steam Sealed Valves, Class 1, 2, and 3 1542 Requirements for Type 403 Modified Forgings or Bars for Bolting Material 1544 Radiographic Acceptance Standards for Repair Welds 1545 Test Specimens from Separate Forgings for Class 1, 2, 3, and MC.

1546 Fracture Toughness Test for Weld Metal Section 1547 Weld Procedure Qualification Tests; Impact Testing Requirements, Class 1 1552 Design by Analysis of Section III Class 1 Valves 1556 Penetrameters for Film Side Radiographs in Table T-320 of Section V 1567 Test Lots for Low Alloy Steel Electrodes 1568 Test Lots for Low Alloy Steel Electrodes 1571 Materials for Instrument Line Fittings; for SA-234 Carbon Steel Fittings 1573 Vacuum Relief Valves 1574 Hydrostatic Test Pressure for Safety Relief Valves 2142 NiCrFe Alloy UNS NO6052 (Unit 2) 2143 NiCrFe Alloy UNS W86152 (Unit 2)

Revision 5209/29/2016 NAPS UFSAR 5.2-50 Table 5.2-2 ASME CODE CASES FOR CLASS 1 COMPONENTS Code Case Title N-20-1 SB-163 NiCrFe Tubing at a Specified Minimum Yield Strength of 40.0 ksi N-401-1 Eddy Current Examination N-411 Alternative Damping Values for Seismic Analysis of Classes 1, 2, and 3 Piping Sections N-474-1 Design Stress Intensities and Yield Strength Values for UNS N06690 with a Minimum Specified Yield Strength of 35.0 ksi N-474-2 Design Stress Intensities and Yield Strength Values for UNS N06690 with a Minimum Specified Yield Strength of 35 ksi, Class 1 Components,Section III, Division 1 2142-1 F-Number Grouping for NiCrFe, Classification UNS N06052 Filler Metal Section IX 2143-1 F-Number Grouping for NiCrFe, Classification UNS W86152 Welding Electrode Section IX

Table 5.2-3 EQUIPMENT CODE AND CLASSIFICATION LIST ANS Safety Code Component Class Code Class Edition and Addenda Reactor coolant system Reactor vessela 1 ASME III A 1968 Edition through Winter 1968 Addenda Control rod drive mechanism housing 1 ASME III A 1968 Edition through Winter 1969 Addenda Steam generatorb Revision 5209/29/2016 Tube side 1 ASME III A 1968 Edition through Winter 1968 Addenda Shell side 2c ASME III Ac 1968 Edition through Winter 1968 Addenda Reactor coolant stop valvesd 1 ASME III A 1968 Edition through Summer 1969 Addenda Pressurizer 1 ASME III A 1968 Edition through Winter 1968 Addenda Reactor coolant piping, fittings, and fabricatione 1 USAS B31.7 1f, g 1969 Surge pipe, fittings, and fabrication 1 USAS B31.7 1f, g 1969 Loop bypass line 1 USAS B31.7 N/A 1969 Loop stop valvesd 1 ASME III A 1968 Edition through Winter 1968 Addenda Reactor coolant thermowellse 1 USAS B31.7 N/A Safety valves 1 ASME III A 1968 Edition through Winter 1968 Addenda Relief valves 1 ANSI B16.5 N/A 1968 Edition through Winter 1968 Addenda Valves to reactor coolant pressure boundary 1 USAS B31.7, B16.5 N/A MSS-SP-65 1968 Edition or ASME III Pressurizer relief tank NNS ASME VIII UW Key: NNS = nonnuclear safety

a. The Reactor Vessel Closure Heads were Fabricated and Manufactured in accordance with the French Construction Code (R-CCM) 1993 Edition with, 1st Addenda June 1994, 2nd Addenda June 1995, 3rd Addenda June 1996 and Modification Sheets FM 797, 798, 801, 802, 803, 804, 805, 806, and 807. The sizing calculations and the stress and fatigue analysis were performed to ASME B&PV Code,Section III, 1995 Edition 1996 Addenda. The Design Reports certified that the closure heads meet the design requirements and stress limits for the ASME B&PV Code,Section III, 1968 Edition through NAPS UFSAR Winter 1968 Addenda.
b. Code edition is for Class I Stress Reports. Replacement steam generators were fabricated and manufactured in accordance with the 1986 Edition of ASME III.
c. Code design requirements assigned are in excess of the requirement dictated by the applicable Safety Class.
d. The only ASA B31.1 Code Case applied for valves within the reactor coolant system was Code Case N-10, liquid penetrant acceptance standards for cast materials. The purchase order dates for the valves varied from February 1969 through February 1971. A complete discussion of Code effectivity and applicability for these valves was carried on in the PSAR stage of review, reference AEC question 4.32. At that time, it was determined that the codes applied in the construction of the valves were adequate. (Reference pages 13 and 14 of the Safety Evaluation Report, dated October 14, 1970.) The analyses of loop stop valves is based on 1968 Edition through Summer 1969 for MUR uprate conditions.
e. Reactor coolant system narrow range RTD thermowells and RVLIS pipe connections on the reactor coolant hot leg piping were installed under the RTD Bypass Line Elimination Projects. The thermowells and piping connections are designed in accordance with ASME Section III-1980 requirements and reconciled to the Original Construction Code.
f. The purchase order date for the reactor coolant system piping was April 30, 1969. The purchase order date for the reactor coolant system fittings was December 24, 1969.
g. Additional information is provided in Section 3.2.2.

5.2-51

Table 5.2-3 (continued)

EQUIPMENT CODE AND CLASSIFICATION LIST ANS Safety Code Component Class Code Class Edition and Addenda Control rod drive mechanism head adaptor plugs 1 ASME III 1 1995 Edition with 1996 Addenda Reactor coolant system (continued)

Core exit thermocouple nozzle assembly 1 ASME III 1 1989 Edition with no Addenda Reactor coolant pump 1-RC-P-1C standpipe orifice NNS No code -

Revision 5209/29/2016 Reactor coolant pump 1-RC-P-1C standpipe NNS ASME VIII -

Reactor coolant pump Reactor coolant pump casing 1 ASME III 1968 Edition through Winter 1970 Addenda Main flange 1 ASME III A 1968 Edition through Winter 1970 Addenda Thermal barrier 1 ASME III A 1968 Edition through Winter 1970 Addenda 1-RC-P-1A & -1B; 2-RC-P-1A, 1B, & 1C seal housing 1 ASME III A 1968 Edition through Winter 1970 Addenda No. 1 Seal housing 1-RC-P-1C 1 ASME III A 1968 Edition through Winter 1970 Addenda No. 2 seal housing 1-RC-P-1C 2d ASME III Ac 1968 Edition through Winter 1970 Addenda Pressure retaining bolting 1 or 2d ASME III A 1968 Edition through Winter 1970 Addenda Remaining parts NNS ASME III 1968 Edition through Winter 1970 Addenda Vent System Vessel vent piping and fittings up to orifices - ANSI B31.7 1 Vessel vent piping and fittings after orifices - ANSI B31.7 2 Pressurizer vent piping and fittings up to orifice - ANSI B31.7 1 Key: NNS = nonnuclear safety

a. The Reactor Vessel Closure Heads were Fabricated and Manufactured in accordance with the French Construction Code (R-CCM) 1993 Edition with, 1st Addenda June 1994, 2nd Addenda June 1995, 3rd Addenda June 1996 and Modification Sheets FM 797, 798, 801, 802, 803, 804, 805, 806, and 807. The sizing calculations and the stress and fatigue analysis were performed to ASME B&PV Code, NAPS UFSAR Section III, 1995 Edition 1996 Addenda. The Design Reports certified that the closure heads meet the design requirements and stress limits for the ASME B&PV Code,Section III, 1968 Edition through Winter 1968 Addenda.
b. Code edition is for Class I Stress Reports. Replacement steam generators were fabricated and manufactured in accordance with the 1986 Edition of ASME III.
c. Code design requirements assigned are in excess of the requirement dictated by the applicable Safety Class.
d. The only ASA B31.1 Code Case applied for valves within the reactor coolant system was Code Case N-10, liquid penetrant acceptance standards for cast materials. The purchase order dates for the valves varied from February 1969 through February 1971. A complete discussion of Code effectivity and applicability for these valves was carried on in the PSAR stage of review, reference AEC question 4.32. At that time, it was determined that the codes applied in the construction of the valves were adequate. (Reference pages 13 and 14 of the Safety Evaluation Report, dated October 14, 1970.) The analyses of loop stop valves is based on 1968 Edition through Summer 1969 for MUR uprate conditions.
e. Reactor coolant system narrow range RTD thermowells and RVLIS pipe connections on the reactor coolant hot leg piping were installed under the RTD Bypass Line Elimination Projects. The thermowells and piping connections are designed in accordance with ASME Section III-1980 requirements and reconciled to the Original Construction Code.
f. The purchase order date for the reactor coolant system piping was April 30, 1969. The purchase order date for the reactor coolant system fittings was December 24, 1969.
g. Additional information is provided in Section 3.2.2. 5.2-52

Table 5.2-3 (continued)

EQUIPMENT CODE AND CLASSIFICATION LIST ANS Safety Code Component Class Code Class Edition and Addenda Pressurizer vent piping and fittings after orifice - ANSI B31.7 2 Isolation valves - ASME III 1 1977 Key: NNS = nonnuclear safety Revision 5209/29/2016

a. The Reactor Vessel Closure Heads were Fabricated and Manufactured in accordance with the French Construction Code (R-CCM) 1993 Edition with, 1st Addenda June 1994, 2nd Addenda June 1995, 3rd Addenda June 1996 and Modification Sheets FM 797, 798, 801, 802, 803, 804, 805, 806, and 807. The sizing calculations and the stress and fatigue analysis were performed to ASME B&PV Code,Section III, 1995 Edition 1996 Addenda. The Design Reports certified that the closure heads meet the design requirements and stress limits for the ASME B&PV Code,Section III, 1968 Edition through Winter 1968 Addenda.
b. Code edition is for Class I Stress Reports. Replacement steam generators were fabricated and manufactured in accordance with the 1986 Edition of ASME III.
c. Code design requirements assigned are in excess of the requirement dictated by the applicable Safety Class.
d. The only ASA B31.1 Code Case applied for valves within the reactor coolant system was Code Case N-10, liquid penetrant acceptance standards for cast materials. The purchase order dates for the valves varied from February 1969 through February 1971. A complete discussion of Code effectivity and applicability for these valves was carried on in the PSAR stage of review, reference AEC question 4.32. At that time, it was determined that the codes applied in the construction of the valves were adequate. (Reference pages 13 and 14 of the Safety Evaluation Report, dated October 14, 1970.) The analyses of loop stop valves is based on 1968 Edition through Summer 1969 for MUR uprate conditions.
e. Reactor coolant system narrow range RTD thermowells and RVLIS pipe connections on the reactor coolant hot leg piping were installed under the RTD Bypass Line Elimination Projects. The thermowells and piping connections are designed in accordance with ASME Section III-1980 requirements and reconciled to the Original Construction Code.
f. The purchase order date for the reactor coolant system piping was April 30, 1969. The purchase order date for the reactor coolant system fittings was December 24, 1969.
g. Additional information is provided in Section 3.2.2.

NAPS UFSAR 5.2-53

Revision 5209/29/2016 NAPS UFSAR 5.2-54 Table 5.2-4

SUMMARY

OF REACTOR COOLANT SYSTEM DESIGN TRANSIENTS Transients Occurrences Normal conditions Heatup and cooldown at 100°F/hr a, b 200 (each)

(pressurizer cooldown 200°F/hr) c Unit loading and unloading at 5% of full power/min 18,300 (each)

Step-load increase and decrease of 10% of full power 2000 (each)

Large step-load decrease 200 Steady-state fluctuations Infinite Upset conditions Loss of load, without immediate turbine or reactor trip d 80 Loss of power (blackout with natural circulation in the 40 reactor coolant system) e Loss of flow (partial loss of flow one pump only) f 80 Reactor trip from full power g 400 Inadvertent auxiliary spray h 10 Faulted conditions i Main reactor coolant pipe break 1 Steam pipe break 1 Design-basis earthquake 1 Test conditions Turbine roll test 10 Hydrostatic test conditions Primary side 5 Secondary side 5 Primary-side leak test 50

a. Heatup cycleTavg from 200°F to 550°F.
b. Cooldown cycleTavg from 550°F to 200°F.
c. Pressurizer cooldown cycle temperatures from 650°F to 200°F.
d. 15% of RATED THERMAL POWER to 0% of RATED THERMAL POWER.
e. Loss of offsite A.C. electrical power source supplying the onsite engineered safety features (ESF)

Electrical System.

f. Loss of only one reactor coolant pump.
g. 100% to 0% of RATED THERMAL POWER. (Full Power Trip)
h. Spray water temperature differential > 320°F.
i. In accordance with the ASME Nuclear Power Plant Components Code, faulted conditions are not included in fatigue evaluations.

Revision 5209/29/2016 NAPS UFSAR 5.2-55 Table 5.2-5 STEAM GENERATOR PRIMARY/SECONDARY BOUNDARY COMPONENTS Condition: Design Condition Primary/Secondary Pressures = 2485/885 psiga Primary Chamber Design Temperature 650°F Secondary Chamber Design Temperature 600°F Maximum Allowable Location Stress Stress Stress (Figure 5.2-1) Description Category Intensity (ksi) Limit (ksi) 2 Channel Head to Tubesheet PL 17.76 40.05 Junction, in the Channel Head PL+Pb 43.13b 40.05 3 Channel Head to Tubesheet PL 16.82 45.00 Junction, in the Tubesheet PL+Pb 48.10b 45.00 4 Tubesheet to Stub Barrel PL 15.06 40.05 Junction PL+Pb 15.41 40.05

a. Based on 1600 psig Primary to Secondary Design Pressure Differential
b. Exceeds the allowable stress limit. A limit analysis was performed per N-417.6(b) of the ASME Code Section III.

Specified Primary Pressure = 2485 psig 2/3 Lower Bound Collapse Load (Primary Pressure) = 3390 psig Secondary Pressure = 885 psi Table 5.2-6 STEAM GENERATOR PRIMARY/SECONDARY BOUNDARY COMPONENTS Condition: Primary Hydrotest Primary Chamber Hydrotest Pressure 3107 psig Secondary Chamber Hydrotest Pressure 0 psig Test Temperature 70-250°F Maximum Allowable Location Stress Stress Stress (Figure 5.2-1) Description Category Intensity (ksi) Limit (ksi) 2 Channel Head to Tubesheet PL 27.41 62.47 Junction, in the Channel Head PL+Pb 67.21a 62.47 3 Channel Head to Tubesheet PL 28.03 82.42 Junction, in the Tubesheet PL+Pb 75.82 82.42 4 Tubesheet to Stub Barrel PL 22.49 62.47 Junction PL+Pb 42.50 62.47

a. Exceeds the allowable stress limit. A limit analysis was performed per N-417.6(b) of the ASME Code Section III.

Specified Primary Pressure = 3107 psig 2/3 Lower Bound Collapse Load (Primary Pressure) = 3400 psig Secondary Pressure = 0 psi

Revision 5209/29/2016 NAPS UFSAR 5.2-56 Table 5.2-7 STEAM GENERATOR PRIMARY/SECONDARY BOUNDARY COMPONENTS Condition: Secondary Hydrotest Secondary Chamber Hydrotest Pressure 1357 psig Primary Chamber Hydrotest Pressure 0 psig Test Temperature 70-180°F Maximum Allowable Location Stress Stress Stress (Figure 5.2-1) Description Category Intensity (ksi) Limit (ksi) 2 Channel Head to Tubesheet PL 9.20 62.47 Junction, in the Channel Head PL+Pb 18.66 62.47 3 Channel Head to Tubesheet PL 10.00 82.42 Junction, in the Tubesheet PL+Pb 21.63 82.42 4 Tubesheet to Stub Barrel PL 16.53 62.47 Junction PL+Pb 49.12 62.47 Table 5.2-8 STEAM GENERATOR PRIMARY/SECONDARY BOUNDARY COMPONENTS Condition: Faulted Condition, Loss of Secondary Side Pressure Primary Chamber Pressure 2485 psig Secondary Chamber Pressure 0 psig Temperature 668°F Maximum Allowable Location Stress Stress Stress (Figure 5.2-1) Description Category Intensity (ksi) Limit (ksi) 2 Channel Head to Tubesheet PL 21.92 36.94 Junction, in the Channel Head PL+Pb 53.76 55.41 3 Channel Head to Tubesheet PL 22.42 50.72 Junction, in the Tubesheet PL+Pb 60.64 76.08 4 Tubesheet to Stub Barrel PL 17.99 36.94 Junction PL+Pb 33.99 55.41

Revision 5209/29/2016 NAPS UFSAR 5.2-57 Table 5.2-9 STEAM GENERATOR PRIMARY/SECONDARY BOUNDARY COMPONENTS Condition: Normal, Upset, and Test Conditions Maximum Location Fatigue (Figure 5.2-1) Description Usage 2 Channel Head to Tubesheet Junction, in the Channel Head 0.03 3 Channel Head to Tubesheet Junction, in the Tubesheet 0.13 4 Tubesheet to Stub Barrel Junction 0.06 Table 5.2-10 STEAM GENERATOR PRIMARY/SECONDARY BOUNDARY COMPONENTS Condition: Normal, Upset, and Test Conditions Description Maximum Location Fatigue (Figure 5.2-1) Usage 1 Tubesheet Center 0.16

Revision 5209/29/2016 NAPS UFSAR 5.2-58 Table 5.2-11 STEAM GENERATOR PRIMARY/SECONDARY BOUNDARY COMPONENTS Location: Tubesheet Center Maximum Stress Allowable Stress Intensity Stress Limit Condition Description Category (ksi) (ksi)

Design Condition 2485 / 885 psig Pm 9.92 30.00 650 / 600°F PL+Pb 46.44a 45.00 Primary Hydrotest 3107 / 0 psig Pm 10.28 54.95 70 - 250°F PL+Pb 81.04 82.42 Secondary Hydrotest 0 / 1357 psig Pm 2.64 54.95 70 - 180°F PL+Pb 33.44 82.42 Faulted Condition (Loss of Secondary Pressure) Pm 8.22 50.72 PL+Pb 64.82 76.08

a. Exceeds the allowable stress limit. A limit analysis was performed per N-417.6 (b) of the ASME Code Section III.

Specified Primary Pressure = 2485 psig 2/3 Lower Bound Collapse Load (Primary Pressure) = 3390 psig Secondary Pressure = 885 psi

Revision 5209/29/2016 NAPS UFSAR 5.2-59 Table 5.2-12 LIMIT ANALYSIS CALCULATIONS RESULTS Case Location Limit Pressure Hot:

Primary/Secondary Pressure Channel/Primary Shell 3185 psi 2485/885 psi Tubesheet/Secondary Shell Tubesheet Center Temperature 650°F Cold Hydro: (Primary Hydrotest)

Primary/Secondary Pressure Channel/Primary Shell 3887 psi 3107/0 psi Tubesheet/Secondary Shell Tubesheet Center Temperature 70°F Cold: (With Secondary Pressure)

Primary/Secondary Pressure Channel/Primary Shell 4401 psi 3107/700 psi Tubesheet/Secondary Shell Tubesheet Center Temperature 70°F Hot Hydro:

Primary/Secondary Pressure Channel/Primary Shell 3354 psi 2485/0 psi Tubesheet/Secondary Shell Tubesheet Center Temperature 400°F Table 5.2-13 LOAD COMBINATIONS AND OPERATING CONDITIONS Load Combination Operating Condition Normal (deadweight, thermal, and pressure) Normal Normal and operating-basis earthquake Upset Normal and design-basis earthquake Faulted Normal and design-basis earthquake design Faulted basis accident

Revision 5209/29/2016 NAPS UFSAR 5.2-60 Table 5.2-14 LOADING CONDITIONS AND STRESS LIMITS: CLASS A COMPONENTS Loading Conditions Stress Intensity Limits Note Design (a) Pm < Sm condition (b) PL < 1.5 Sm (c) Pm (or PL) + PB < 1.5 Sm 1 Normal and (a) Pm (or PL) + PB + Q < 3.0 Sm 2 Upset condition (b) Cumulative Fatigue Usage < 1.0 Faulted (a) Pm < 1.2 Sm or Sy, whichever is larger, PL < 1.5 (1.2) Sm or 3 condition 1.5 Sy, whichever is larger, and Pm (or PL) + PB < 1.5 (1.2) Sm or 1.5 Sy, whichever is larger, or (b) Faulted condition limits in Table 5.2-16 Key: Pm= primary general membrane stress intensity PL = primary local membrane stress intensity PB = primary bending stress intensity Q = secondary stress intensity Sm = stress intensity value from ASME Code,Section III Sy = minimum specified material yield from ASME Code,Section III, Table N-421 or equivalent.

Notes:

1. The limits on local membrane stress intensity (PL < 1.5 Sm) and primary membrane plus primary bending stress intensity (Pm (or PL) +PB < 1.5 Sm) need not be satisfied at a specific location if it can be shown by means of limit analysis or by tests that the specified loadings do not exceed two-thirds of the lower bound collapse load per paragraph N-417.6(b) of the ASME Code,Section III.
2. In lieu of satisfying the specific requirements for local membrane (PL < 1.5 Sm) or the primary plus secondary stress intensity (Pm (or PL) + PB + Q < 3 Sm) at a specific location, the structural action may be calculated on a plastic basis and the design will be considered to be acceptable if shakedown occurs, as opposed to continuing deformation, and if the deformations that occur before shakedown do not exceed specified limits per paragraph N-417.6(a)(2) of the ASME Code,Section III.
3. The limits on local membrane stress intensity (PL < 1.85 Sm or 1.5 Sy) need not be satisfied at a specific location if it can be shown by means of limit analysis or by test that the specified loadings do not exceed 120% of two-thirds of the lower bound collapse load per paragraph N-417.10(c) of the ASME Code,Section III.

Revision 5209/29/2016 NAPS UFSAR 5.2-61 Table 5.2-15 LOADING CONDITIONS AND STRESS LIMITS: NUCLEAR POWER PIPINGa Loading Conditions Stress Intensity Limits Normal condition (a) Pm Sm (b) PL 1.5 Sm (c) Pm (or PL) + PB 1.5 Sm (d) Pm (or PL) + PB + Pe + Q 3.0 Sm (e) Pe 3.0 Sm Upset condition (a) Pm Sm (b) PL 1.5 Sm (c) Pm (or PL) + PB 1.5 Sm (d) Pm (or PL) + PB + Pe + Q 3.0 Sm (e) Pe 3.0 Sm Faulted condition Faulted condition limits as shown in Table 5.2-16 Key: Pm = primary general membrane stress intensity PL = primary local membrane stress intensity PB = primary bending stress intensity Pe = secondary expansion stress intensity Q = secondary membrane plus bending stress intensity Sm = allowable stress intensity from USAS B31.7 Code for Nuclear Power Piping

a. Alternatively, the rules and simplified analysis of Divisions I-704 and I-705 with the stress limits defined by Code Case 70 of USAS B31.7 may be used in lieu of these equations.

Table 5.2-16 FAULTED CONDITION STRESS LIMITS FOR CLASS A COMPONENTS Stress Limits for Components System (or Subsystem)

Analysis Component Analysis Pm Pm + Pb Test Elastic Elastic Smaller of 2.4 Sm and 0.70 Su Smaller of 3.6 Sm and 1.05 Sua b

Plastic Larger of 0.70 Su or Sy + 1/3 (Su - Sy) Larger of 0.70 Sut or Sy + 1/3 (Sut - Sy) 0.8 LT Revision 5209/29/2016 (b)

Limit analysis 0.9 L1 (b) (c)

(d)

Plastic Plastic or elastic Larger of 0.70 Su or Sy + 1/3 (Su - Sy) Larger of 0.70 Sut or Sy + 1/3 (Sut - Sy)

Key: Sy= yield stress at temperature Su= ultimate stress from engineering stress-strain curve at temperature Sut= ultimate stress from true stress-strain curve at temperature Sm= stress intensity from ASME Code Section III, at temperature

a. These limits are based on a bending shape factor of 1.5 for simple bending; for cases with different shape factors, the limits will be changed proportionally.
b. When elastic system analysis is performed, the effect of component deformation on the dynamic system response should be checked.
c. LT = The limits established for the analysis, etc. The limits established for the analysis need not be satisfied if it can be shown from the test of a prototype or model that the specified loads (dynamic or static equivalent) do not exceed 80% of LT, where LT is the ultimate load or load combination used in the test. In using this method, account shall be taken of the similitude relationships that may exist between the actual component and the tested models to ensure that the loads obtained from the test are a conservative representation of the load carrying capability of the actual component under postulated loading for faulted conditions.
d. L1 = lower bound limit load with an assumed yield point equal to 2.3 Sm.

NAPS UFSAR 5.2-62

Revision 5209/29/2016 NAPS UFSAR 5.2-63 Table 5.2-17 FAULTED CONDITION LOADS FOR THE REACTOR COOLANT PUMP FEET Fx Fy Fz Mxa Mya Mza W Umbrella +3305 +3400 +2605 +7059 +4010 +7083 Case 1b - 390 294 - - -

Case 2b - 521 330 - - -

Case 3b - 959 376 - - -

Case 4b - 527 326 - - -

a. No moments are transmitted to the pump feed due to the specific design of the supports.
b. These four cases represent the largest loading conditions on pump feet.

Case 1: Deadweight + Thermal + Internal Pressure + SRSS (SSE & main steam line break)

Case 2: Deadweight + Thermal + Internal Pressure + SRSS (SSE & residual heat removal line break)

Case 3: Deadweight + Thermal + Internal Pressure + SRSS (SSE & accumulator/safety injection line break)

Case 4: Deadweight + Thermal + Internal Pressure + SRSS (SSE & pressurizer surge line break)

Table 5.2-18 OPERATING AND INACTIVE VALVES IN THE REACTOR COOLANT SYSTEM BOUNDARY Line Valve Typea Normal Position Post-LOCA Position RHR suction 1. Motor gate I Closed (interlocked with Closed RCS pressure)

2. Motor gate I Closed (interlocked with Closed Revision 5209/29/2016 RCS pressure)

Loop drains (each 1. Manual globe I Closed Closed loop) 2. Air-op globe Closed Closed Charging 1. Check O Open Closed

2. Air-op globe O Open Closed RHR return (each 1. Check O Closed Open - for accumulator injection of two loops) 2. Motor gate I Closed Closed Accumulator 1. Check O Closed Open - for accumulator injection
2. Check O Closed Open - for accumulator injection SIS - boron 1. Check O Closed Open - for boron high-head and low-head injection injection tank (each 2. Check O Closed Open - for boron and high-head injection loop)

Hot-leg 1. Check O Closed Open - for hot-leg recirculation NAPS UFSAR connections (each 2. Manual globe I Open Open loop) 3. Check O Closed Open - for hot-leg recirculation Excess letdown 1. Air-op globe Ob Closed (fail close) Closed Letdown 1. Manual globe I Open Open

a. O = operating; I = inactive.
b. There is a possibility for these valves to be open when the accident occurs.

5.2-64

Table 5.2-18 (continued)

OPERATING AND INACTIVE VALVES IN THE REACTOR COOLANT SYSTEM BOUNDARY Line Valve Typea Normal Position Post-LOCA Position

2. Air-op globe O Open (fail close) Closed - on low pressurizer level signal
3. Air-op globe O Open (fail close) Closed - on low pressurizer level signal Low-head injection 1. Check O Closed Open - for low-head injection and recirculation
2. Check O Closed Open - for low-head injection and recirculation Revision 5209/29/2016 Pressurizer relief 1. Motor gate I Open Open valves (to PRT) 2. Air-op globe I Closed (fail close) Closed (fail close)

Pressurizer safety 1. Safety valve O Closed Closed valves (to PRT)

Auxiliary spray 1. Check Ob Closed Closed (from CVCS) 2. Air-op globe Ob Closed (fail close) Closed

a. O = operating; I = inactive.
b. There is a possibility for these valves to be open when the accident occurs.

NAPS UFSAR 5.2-65

Table 5.2-19 ACTIVE VALVES IN THE REACTOR COOLANT PRESSURE BOUNDARY Active Design Operating Functional Assurance of Active Mark Number a Valve Function Position Condition Condition Tests b Function 1-CH-LCV-1460A, B Letdown line Closed 2485 psig 2235 psig (c) Fails closed (d) 650°F 533°F 1-CH-HCV-1200A, B, C Letdown line orifice isolation Closed 2485 psig 300 psig (c) Fails closed and closes Revision 5209/29/2016 650°F 290°F on SI signal 1-CH-TV-1204A, B Letdown line containment Closed 600 psig 300 psig (c) Fails closed and closes isolation 400°F 290°F on SI signal 1-CH-MOV-1380 and 1381 Seal return isolation Closed 200 psig 50 psig (e) Closes on CIA signal 250°F 170°F 1-CH-MOV-1289A Charging isolation Closed 2485 psig 2485 psig (e) Closes on SI signal (d) 650°F 130°F 1-SI-MOV-1867C, D Boron injection tank Open 2485 psig 2485 psig (e) Opens on SI signal (d) containment isolation 650°F 180°F 1-SI-MOV-1869A, B Hot leg isolation Open 2485 psig 2485 psig (e) Opened manually for 650°F 180°F recirculation 1-SI-MOV-1836 Cold leg isolation Open 2485 psig 2485 psig (e) Opened manually for 650°F 180°F recirculation 1-SI-MOV-1890C, D LHSI cold leg isolation Closed 2485 psig 100 psig (e) Closed manually for NAPS UFSAR 650°F 180°F recirculation 1-SI-MOV-1890A, B LHSI hot leg isolation Open 2485 psig 100 psig (e) Opened manually for 650°F 180°F recirculation

a. Unit 1 equipment is listed. Unit 2 equipment is similar.
b. Performed by manufacturer.
c. Shell hydrostatic, seat leakage (done with zero pressure on air operator for fail-closed valves), and backseat leakage.
d. Valves that automatically operate on SI or containment isolation phase A (CIA) signal are redundant to ensure completion of function.
e. Shell hydrostatic, seat leakage, backseat leakage.

5.2-66

Revision 5209/29/2016 NAPS UFSAR 5.2-67 Table 5.2-20 RTPTS VALUES FOR NORTH ANNA UNIT 1 a 50.3 EFPY Vessel Material RTPTS Values (°F) Screening Criteria (°F)

Forging 03 (Lower Shell 190.9 270 Forging)

Forging 04 (Intermediate 174.3 270 Shell Forging)

Forging 05 (Nozzle Shell 145.7 270 Forging)

Weld 04 (Intermediate to 155.6 300 Lower Shell Weld)

Weld 05A (Nozzle to 132.8 300 Intermediate Shell; OD 94%)

Weld 05B (Nozzle to 120.8 300 Intermediate Shell; ID 6%)

a. References 17 and 26.

Note: This table reflects results for a cumulative core burnup of 50.3 EFPY which corresponds to the estimated cumulative core burnup at the end of the 60-year license period assuming a 90% capacity factor for cycles beyond Cycle 10.

Table 5.2-21 RTPTS VALUES FOR NORTH ANNA UNIT 2 a 52.3 EFPY Vessel Material RTPTS Value (°F) Screening Criteria (°F)

Forging 03 (Lower Shell 227.7 270 Forging)

Forging 04 (Intermediate 186.6 270 Shell Forging)

Forging 05 (Nozzle Shell 106.8 270 Forging)

Weld 04 (Intermediate to 18.5 300 Lower Shell Weld)

Weld 05A (Nozzle to 123.4 300 Intermediate Shell; OD 94%)

Weld 05B (Nozzle to 118.5 300 Intermediate Shell; ID 6%)

a. References 18 and 26.

Note: This table reflects results for a cumulative core burnup of 52.3 EFPY which corresponds to the estimated cumulative core burnup at the end of the 60-year license period assuming a 90% capacity factor for cycles beyond Cycle 10.

Revision 5209/29/2016 NAPS UFSAR 5.2-68 Table 5.2-22 REACTOR COOLANT PRESSURE BOUNDARY MATERIALS Component Type Reactor vessel components Shell and lower head plates (other SA-533 Grade A, B, or C; Class 1 or 2 (vacuum than core region) treated)

Shell, flange and nozzle forgings SA-508 Class 2 or 3 Nozzle safe ends SA-182 Type F304 or F316 weld buildup Closure head dome 16 MND 5 (RCC-M Spec. M2122)

(ASME Equivalent Material SA-533 Type B Class 1)

Closure head flange 16 MND 5 (RCC-M Spec. M2113)

(ASME Equivalent Material SA-508 Grade 3 Class 1)

CRDM nozzle adapters Z2 CN 19-10 (RCC-M Spec. M3301)

(ASME Equivalent Material SA-182 F304)

CRDM sleeves NC 30 Fe (RCC-M Spec. M4108)

(ASME Equivalent Material SB-167 UNS N06690, Alloy 690)

CRDM nozzle plug SA-182 Grade F304 Vent pipe nozzle NC 30 Fe (RCC-M Spec. M4109)

(ASME Equivalent Material SB-166 UNS N06690, Alloy 690 Closure head NC Fe welding INCO ALLOY 152 (ASME Equivalent Material materials SFA-5.11 Code Case 2143-1, UNS W86152)

INCO ALLOY 52 (ASME Equivalent Material SFA-5.14, Code Case 2142-1, UNS N06052)

Instrument tube appurtenances - SA-182 Type F304, F304L or F316 (safe ends) lower head Alloy 600 ASME SB-166 Closure studs, nuts, and washers SA-540 Class 3 Grade B23 or B24 Core support pads SB-166 with carbon less than 0.10%

Monitor tubes SA-312 Type 304 Vessel supports, seal ledge SA-516 Grade 70 quenched and tempered or SA-533 Grade A, B, or C: Class 1 or 2 (vessel supports may be of weld metal buildup of equivalent strength)

Cladding (Closure Head) 1st layer SS Type ER309L and SS Type ER308L for subsequent layers Cladding other than Closure Head Stainless steel weld metal analysis A-7 and Ni-Cr-Fe weld metal F-Number 43

Revision 5209/29/2016 NAPS UFSAR 5.2-69 Table 5.2-22 (continued)

REACTOR COOLANT PRESSURE BOUNDARY MATERIALS Component Type Reactor vessel components (continued)

Head lifting lugs 18 MND 5 (RCC-M Spec. M2125)

(ASME Equivalent Material SA-533 Type B Class 1)

Steam generator components (Unit 1 and Unit 2 Replacement)

Lower assembly shell ASME SA-508, Class 3 Forging Transition cone (below girth weld) ASME SA-508, Class 3 Forging Transition cone (above girth weld) ASME SA-533, Grade A Class 1 Plate and Upper Assembly Shell Tubesheet ASME-SA-508, Class 3 Forging Channel head ASME SA-508, Class 3 Forging Support plates ASME SA-240, Type 405 Channel head cladding ASME SFA-5.4, Class E309L (1st Layer)

ASME SFA-5.4, Class E308L (Remaining Layers)

Tubesheet Cladding ASME SFA-5.14, Class ERNiCr-3 Tubes ASME SB-163, Alloy 690 TT Primary Nozzle Safe Ends ASME SA-336, Class F316LN Forgings Closure bolting Primary side:

Studs: ASME SA-193 Gr. B7 Nuts: ASME SA-194 Gr. 7 (16 each per manway - specially designed for use with hydraulic stud tensioner)

Secondary Side:

Heavy Hex Bolts: ASME SA-193 Gr. B7 OR Studs: ASME SA-193 Gr. B7 with Nuts: ASME SA-194 Gr. 7 Nuts (20 of the same type fasteners per manway)

Pressurizer components Pressure plates SA 533 Grade A, B, or C; Class 1 or 2 Pressure forgings SA 508 Class 2 or 3 Nozzle safe ends SA 182 or 376 Type F316 or 316L and Ni-Cr-Fe weld metal F-Number 43 Cladding Stainless steel weld metal analysis A-7 and Ni-Cr-Fe weld metal F-Number 43

Revision 5209/29/2016 NAPS UFSAR 5.2-70 Table 5.2-22 (continued)

REACTOR COOLANT PRESSURE BOUNDARY MATERIALS Component Type Pressurizer components (continued)

Closure bolting ASTM A193 Gr. B7 Studs with ASTM A194 Gr. 7 or 2H Heavy-Hex Nuts OR ASTM A193 Gr. B7 Bolts Pressurizer safety valve forgings SA 182 Type F316 or F347 Reactor coolant stop valves Body and bonnet SA 351 Grade CF8M Stem SA 564 Grade 630 cond 1100°F heat treatment Closure bolting and nuts SA 540 Grade B24 SA/ASTM-A-194 Grade 2H, SA/ASTM-A-194 Grade 7 Reactor coolant pump Pressure forgings SA 182 Type 304, 316, or 348 Pressure casting SA 351 Grade CF8, CF8A, or CF8M Tube and pipe SA 213, SA 376, or SA 312 - seamless Type 304 or 316 Pressure plates SA 240 Type 304 or 316 Bar material SA 479 Type 304 or 316 Closure bolting SA 193 Grade B7 or B8 SA 540 Grade B23 or 24 SA 453 Grade 660 Flywheel SA 533 Grade B, Class 1 Reactor coolant piping Reactor coolant pipe Code Case 1423-1 Grade F302N or 316N, or SA 351 Grade CF8A or CF8M centrifugal castings Reactor coolant fittings SA 351 Grade CF8A or CF8M Branch nozzles SA 182 Grade F304 or 316 or Code Case 1423-1 Grade F304N or 316N Surge line and loop bypass SA 376 Type 304 or 316 or Code Case 1423-1 Grade F304N or 316N

Revision 5209/29/2016 NAPS UFSAR 5.2-71 Table 5.2-22 (continued)

REACTOR COOLANT PRESSURE BOUNDARY MATERIALS Component Type Reactor coolant piping (continued)

Auxiliary piping 0.5 inch through ANSI B36.19 12 inches and wall schedules 40S through 80S (ahead of second isolation valve)

All other auxiliary piping (ahead of ANSI B36.10 second isolation valve)

Socket weld fittings ANSI B16.11 Piping flanges ANSI B16.5 Auxiliary piping valves (Class I) SA 182 Type 304 or 316 or SA 351 Grade CF8, CF8A, or CF8M Welding materials SFA 5.4 and 5.9 Type 308 or 308L Control rod drive mechanism Pressure housing SA 182 Grade F304 or SA 351 Grade CF8 Pressure forgings SA 182 Grade F304 or SA 336 Grade F8 Bar material SA 479 Type 304 Welding materials SFA 5.4 and 5.9 Type 308 or 308L Part-length mechanism Pressure housing SA 182 or SA 312 seamless Grade 304 and Code Case 1337-5 AISI 403 CRES tempered at 1125+/-25°F may be used in the motor section of the pressure housing, provided it is welded to F-304 end members.

Bar material SA 479 Type 304 Welding materials SFA 5.4 and 5.9 Type 309 or 308L

Revision 5209/29/2016 NAPS UFSAR 5.2-72 Table 5.2-23 REACTOR COOLANT PRESSURE BOUNDARY MATERIALS AUXILIARY COMPONENTS Component Type Motor- and Manual-Operated Gate, Globe and Check Valves Bodies, bonnets, and disks SA 182 Grade F316 or SA 351CF8M Stems SA 564 Type 630 cond. 1,100°F heat treatment Closure bolting and nuts SA 453 Grade 660 and SA 194 Grade B6 or SA 564 Grade 630 H1100 and SA 194 Grade 6 Air-Operated Valves Bodies and bonnets SA 182 Type F316 or SA 351 Grade CF8 or CF8M Disks and stems SA 182 Type F316 or SA 564 Grade 630 cond.

1,100°F heat treatment Closure bolting and nuts SA 453 Grade 660 and SA 194 Grade B6 Auxiliary Relief Valves Forgings SA 182 Type F316 Disk SA 479 Type 316 Miscellaneous Valves (2 in. and smaller)

Bodies and bonnets SA 479 Type 316 or SA 351 Grade CF8 Disks SA 479 Type 316 Stems SA 479 Type 410 or Type 304 Closure bolting and nuts SA 453 Grade 660 and SA 193 Grade B6 Auxiliary Heat Exchangers Heads SA 182 Grade F304 or SA 240 Type 304 or 316 Flanges SA 182 Grade F304 or F316 Flange necks SA 182 Grade F304 or SA 240 Type 316 or SA 312 Type 304 seamless Tubes SA 213 Type 304 Tubesheets SA 240 Type 304 or 316 or SA 182 Grade F304 or SA 515 Grade 70 with stainless steel weld metal analysis A-7 cladding Shells SA 351 Grade CF8 Pipe SA 312 Type 304 seamless

Revision 5209/29/2016 NAPS UFSAR 5.2-73 Table 5.2-23 (continued)

REACTOR COOLANT PRESSURE BOUNDARY MATERIALS AUXILIARY COMPONENTS Component Type Auxiliary Pressure Vessels, Tanks, Filters, etc.

Shells and heads SA 240 Type 304 or SA 264 Type 304 clad to SA 516 Grade 70 or SA 516 Grade 70 with stainless steel weld metal analysis A-7 cladding Flanges and nozzles SA 182 Grade F304 and SA 105 or SA 350 Grade LF2 with stainless steel weld metal analysis A-7 cladding Piping SA 312 Type 304 or Type 316 seamless Pipe fittings SA 403 WP304 seamless Closure bolting and nuts SA 193 Grade B7 or B8 and SA 194 Grade 2H, ASTM A-193 Grade B7 or B16, ASTM A-194 Grade 2H or 7 Auxiliary Pumps Pump casing and heads SA 351 Grade CF8 or CF8M, SA 182 Grade F304 or F316 Flanges and nozzles SA 182 Grade F304 or F316, SA 403 Grade WPS316L seamless Piping SA 312 Type 304 or Type 316 seamless Stuffing or packing box cover SA 351 Grade CF8 or CF8M, SA 240 Type 304 or Type 316 Pipe fittings SA 403 Grade WP316L seamless Closure bolting and nuts SA 193 Grade B6, B7, or B8M and SA 194 Grade 2H or Grade 8M

Revision 5209/29/2016 NAPS UFSAR 5.2-74 Table 5.2-24 REACTOR VESSEL INTERNALS FOR EMERGENCY CORE COOLING Component Type Forgings SA 182 Type F304 Plates SA 240 Type 304 Pipes SA 312 Type 304 seamless or SA 376 Type 304 Tubes SA 213 Type 304 Bars SA 479 Type 304 and 410 Castings SA 351 Grade CF8 or CF8A Bolting SA pending Westinghouse PF Spec 70041EA Nuts SA 193 Grade B-8 Locking devices SA 479 Type 304 Weld buttering Stainless steel weld metal analysis A-7

Revision 5209/29/2016 NAPS UFSAR 5.2-75 Table 5.2-25 REACTOR COOLANT WATER CHEMISTRY SPECIFICATION Parameter Limit Electrical conductivity Dependent on the concentration of boric acid and alkali present. Expected range is less than 1 to 60 mhos/cm at 25°C.

Solution pH Dependent on the concentration of boric acid and alkali present. Expected values range between 4.2 (high boric acid concentration) to 10.5 (low boric acid concentration) at 25°C.

Oxygen, maximum(1) 0.1 ppm Chloride, maximum 0.15 ppm Fluoride, maximum 0.15 ppm Hydrogen(2) (3) 25 to 50 cc(STP)/kg H2O Suspended solids, maximum 0.200 ppm pH control agent (Li7OH) Variable consistent with fuel vendor guidance (4)

Boric acid, ppm B Variable from 0 to approximately 4000 ppm

1. Limit not applicable with Tave 250°F
2. To assist reactor coolant regasing, the reactor coolant dissolved hydrogen concentration may range between 15 to 50 cc/kg within 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> prior to shutdown
3. Due to the effects of dilution during start-up, the reactor coolant hydrogen concentration may range between 15 to 50 cc/kg for 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> following reactor criticality.
4. RCS pH control is determined on a cycle by cycle basis based on fuel vendor guidance and documented in the cycle Reload Safety Evaluation.

The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

Table 5.2-26 PRE-IRRADIATION REACTOR VESSEL TOUGHNESS TABLE (UNIT 1)

Minimum Temperature (°F) Average Upper Shelf for 50 ft-lb (ft-lb)

Parallel to Normal to Parallel to Normal to Major Major Major Major Revision 5209/29/2016 Material NDTT Working Working RTNDT Working Working Component Heat No. Type CU (%) P (%) (°F) Direction Direction (°F) Directiona Direction Closure head 7094 A533,B,Cl.1 -31 -31 dome RCC-M 16MND5 (M2122)

Closure head E4483 - A508,GR.3, -76 -76 flange E4484 CL.1 RCC-M 16MND5 (M2113)

Vessel flange 4982 A508,Cl.2 -22 -70 -50b -22 161 Inlet nozzle 4964 A508,Cl.2 -31 14 34b -26 106 Inlet nozzle 4966 A508,Cl.2 -22 10 30b -22 88 Inlet nozzle 4968 A508, Cl.2 -22 43 63b 3 80 NAPS UFSAR Outlet nozzle 4963 A508,Cl.2 -13 43 63b -3 100 Outlet nozzle 4965 A508,Cl.2 -22 14 34b -22 90 Outlet nozzle 4967 A508,Cl.2 -4 34 54b -4 90 Upper shell 4952 A508,Cl.2 2 46 66b 6 60

a. Minimum energy at highest test temperature (68°F) -% shear not reported.
b. Estimated temperature based on NRC Regulatory Standard Review Plan, Branch Technical Position MTEB 5-2 5.2-76

The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

Table 5.2-26 (continued)

PRE-IRRADIATION REACTOR VESSEL TOUGHNESS TABLE (UNIT 1)

Minimum Temperature (°F) Average Upper Shelf for 50 ft-lb (ft-lb)

Parallel to Normal to Parallel to Normal to Major Major Major Major Material NDTT Working Working RTNDT Working Working Revision 5209/29/2016 Component Heat No. Type CU (%) P (%) (°F) Direction Direction (°F) Directiona Direction Intermediate 4958 A508,Cl.2 0.12 0.009 -31 20 77c 17c 94 92c shell Lower shell 4979 A508,Cl.2 0.16 0.019 -13 40 98c 38c 74 85c Bottom head 53647-3 A533,B, -31 27 47b -13 65.5 segment Cl.1 Bottom head 53648-4 A533,B,Cl.1 -13 27 47b -13 77 segment Bottom head 53774 A533,B, -22 32 52b -8 67 dome Cl.1 Weld Weld 0.086 0.020 -13 79 19 102 Heat- HAZ -22 39 -21 142 affected zone NAPS UFSAR

a. Minimum energy at highest test temperature (68°F) -% shear not reported.
b. Estimated temperature based on NRC Regulatory Standard Review Plan, Branch Technical Position MTEB 5-2
c. Average transverse data obtained from surveillance program.

5.2-77

The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

Table 5.2-27 PRE-IRRADIATION REACTOR VESSEL TOUGHNESS TABLE (UNIT 2)

Minimum Temperature (°F) Average Upper Shelf for 50 ft-lb (ft-lb)

Parallel to Normal to Parallel to Normal to Major Major Major Major Revision 5209/29/2016 Material NDTT Working Working RTNDT Working Working Component Heat No. Type CU (%) P (%) (°F) Direction Direction (°F) Directiona Direction Closure head 7538 A533,B, -22 -22 dome Cl.1 RCC-M 16MND5 (M2122)

Head flange H1681 - A508, -49 -49 H1682 Grade 3,Cl.1 RCC-M 16MND5 (M2113)

Vessel flange 523000 A508,Cl.2 -22 -41 -21b -22 146 Inlet nozzle 990426 A508,Cl.2 -40 60 80b 20 72 Inlet nozzle 54567-2 A508,Cl.2 -31 53 73b 13 118 NAPS UFSAR Inlet nozzle 54590-2 A508,Cl.2 -31 19 39b -21 92 Outlet nozzle 990426-22 A508,Cl.2 -13 41 61b 1 80 Outlet nozzle 990426-3 A508,Cl.2 -31 43 63b 3 62 Outlet nozzle 791291 A508,Cl.2 -22 21 41b -19 115

a. Average energy at highest test temperature (68°F) -% shear not reported.
b. Estimated temperature based on NRC Regulatory Standard Review Plan, Branch Technical Position MTEB 5-2 5.2-78

The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

Table 5.2-27 (continued)

PRE-IRRADIATION REACTOR VESSEL TOUGHNESS TABLE (UNIT 2)

Minimum Temperature (°F) Average Upper Shelf for 50 ft-lb (ft-lb)

Parallel to Normal to Parallel to Normal to Major Major Major Major Material NDTT Working Working RTNDT Working Working Revision 5209/29/2016 Component Heat No. Type CU (%) P (%) (°F) Direction Direction (°F) Directiona Direction Upper shell 990598 A508,Cl.2 0.08 0.010 +5 49 69b 9 86 291396 Intermediate 990496 A508,Cl.2 0.09 0.010 -49 49 135c 75c 85 74c shell 292429 Lower shell 990533 A508,Cl.2 0.13 0.013 -13 31 116c 56c 92 80c 207355 Bottom head 53648-1 A533,B, -22 -9 11b -22 94 segment Cl.1 Bottom head 53648-4 A533,B,Cl.1 -13 31 51b -6 77 segment Bottom head 53695-1 A533,B,Cl.1 -40 21 41b -19 87 dome Weld Weld 0.088 0.017 -67 12 -48 107 NAPS UFSAR Heat affected -49 -20 -49 125 zone

a. Average energy at highest test temperature (68°F) -% shear not reported.
b. Estimated temperature based on NRC Regulatory Standard Review Plan, Branch Technical Position MTEB 5-2
c. Average transverse data obtained from surveillance program.

5.2-79

Revision 5209/29/2016 NAPS UFSAR 5.2-80 The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

Table 5.2-28 PRESERVICE INSPECTION PROGRAM Item Summer Number Category Parts To Be Examined 1975 Reactor Vessel B1.1 B-A Longitudinal and circumferential shell welds in core UT region B1.2 A-B Longitudinal and circumferential welds in shell and UT meridianal and circumferential seam welds in bottom and closure head B1.3 B-C Vessel-to-flange and head-to-flange circumferential UT welds B1.4 B-D Primary nozzle-to-vessel welds and nozzle inside UT radiused section B1.5 B-E Vessel penetrations, including control rod drive and V(IWA 5000) instrumentation penetrations B1.6 B-F Nozzle-to-safe-end welds UT, S B1.7 B-G-1 Closure studs, in place UT B1.8 B-G-1 Closure studs and nuts, when removed UT, S B1.9 B-G-1 Ligaments between threaded stud holes UT B1.10 B-G-1 Closure washers, bushings V B1.11 B-G-2 Pressure-retaining bolting V B1.12 B-H Integrally welded vessel support UT B1.13 B-I-1 Closure head cladding UT or V&S B1.14 B-I-1 Vessel cladding V B1.15 B-N-1 Vessel interior V B1.16 B-N-2 Interior attachments and core support structures V B1.17 B-N-3 Core support structures V

a. Not applicable - nozzles are cast with head and therefore UT is not feasible on inside radiused section.
b. Not applicable - supports cast with head.
c. Use shop radiographs.
d. A UT on integrally welded supports is not feasible at this time.
e. Safe-ends in branch piping welds are not applicable to North Anna.
f. There are no valve body welds at North Anna.
g. There are no integrally welded valve supports at North Anna.
h. The nozzle-to-vessel inside radiused section examination is not feasible at this time
i. IWA-5000
j. Pressure-retaining bolting (B-G-1) is not applicable to North Anna.

Revision 5209/29/2016 NAPS UFSAR 5.2-81 The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

Table 5.2-28 (continued)

PRESERVICE INSPECTION PROGRAM Item Summer Number Category Parts To Be Examined 1975 B1.18 B-O Control rod drive housing UT B1.19 B-P Exempted components V(IWA 5000)

Heat Exchangers and Steam Generators B3.1 B-B Longitudinal and circumferential welds, including UT tubesheet-to-head or tubesheet-to- shell welds on primary side B3.2 B-D Primary nozzle-to-vessel head welds and nozzle-to-head inside radiused section a B3.3 B-F Nozzle-to-safe-end welds UT, S B3.5 & B-G-1 Pressure-retaining bolting UT, S, V 3.6 B3.10 B-G-2 Pressure-retaining bolting V B3.7 B-H Integrally welded vessel supports b B3.8 B-I-2 Vessel cladding V Replacement Steam Generators Unit 1 Summer 1983 B2.40 B-B Tubesheet-to-head and tubesheet-to-shell welds UT B3.140 B-D Nozzle inside radius section UT B5.70 B-F Nozzle-to-safe end welds UT, S B5.130 B-F Dissimilar metal butt welds UT, S B7.30 B-G-2 Pressure retaining bolting V B16.20 B-Q Steam generator tubing ET Unit 2 1986 B2.40 B-B Tubesheet-to-head and tubesheet-to-shell welds UT

a. Not applicable - nozzles are cast with head and therefore UT is not feasible on inside radiused section.
b. Not applicable - supports cast with head.
c. Use shop radiographs.
d. A UT on integrally welded supports is not feasible at this time.
e. Safe-ends in branch piping welds are not applicable to North Anna.
f. There are no valve body welds at North Anna.
g. There are no integrally welded valve supports at North Anna.
h. The nozzle-to-vessel inside radiused section examination is not feasible at this time
i. IWA-5000
j. Pressure-retaining bolting (B-G-1) is not applicable to North Anna.

Revision 5209/29/2016 NAPS UFSAR 5.2-82 The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

Table 5.2-28 (continued)

PRESERVICE INSPECTION PROGRAM Item Summer Number Category Parts To Be Examined 1975 B3.140 B-D Nozzle inside radius section UT B5.70 B-F Nozzle-to-safe end welds UT, S B5.130 B-F Dissimilar metal butt welds UT, S B7.30 B-G-2 Pressure retaining bolting V B16.20 B-Q Steam generator tubing ET Pump Pressure Boundary B5.6 B-L-1 Pump casing welds c UT B5.7 B-L-2 Pump casing V B5.2 & B-G-1 Pressure retaining bolting UT, S, V 5.3 B5.9 B-G-2 Pressure retaining bolting V B5.4 B-K-1 Integrally welded supports d UT B5.5 B-K-2 Supports components V Piping Pressure Boundary B4.1 B-F Safe-end to piping welds and safe-ends in branch UT, S piping welds e B4.2 J-1 Circumferential and longitudinal pipe welds and UT, V branch connections greater than 4 in. diameter B4.7 J-2 Circumferential and longitudinal pipe welds and V branch connection welds B4.8 J-1 Socket welds and pipe branch connection diameter V, S less than or equal to 4 in.

B4.3 & B-G-1 Pressure-retaining bolting UT, S, V B4.4

a. Not applicable - nozzles are cast with head and therefore UT is not feasible on inside radiused section.
b. Not applicable - supports cast with head.
c. Use shop radiographs.
d. A UT on integrally welded supports is not feasible at this time.
e. Safe-ends in branch piping welds are not applicable to North Anna.
f. There are no valve body welds at North Anna.
g. There are no integrally welded valve supports at North Anna.
h. The nozzle-to-vessel inside radiused section examination is not feasible at this time
i. IWA-5000
j. Pressure-retaining bolting (B-G-1) is not applicable to North Anna.

Revision 5209/29/2016 NAPS UFSAR 5.2-83 The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

Table 5.2-28 (continued)

PRESERVICE INSPECTION PROGRAM Item Summer Number Category Parts To Be Examined 1975 B4.12 B-G-2 Pressure-retaining bolting V B4.9 B-K-1 Integrally welded supports UT B4.10 B-K-2 Support components V Valve Pressure Boundary B6.6 B-M-1 Valve body welds f B6.7 B-M-2 Valve bodies V B6.2 & B-G-1 Pressure-retaining bolting UT, S, V B6.3 B6.9 B-G-2 Pressure-retaining bolting V B6.4 B-K-1 Integrally welded supports g B6.5 B-K-2 Support components V Pressurizer B2.1 B-B Longitudinal and circumferential welds UT B2.2 B-D Nozzle-to-vessel welds and nozzle-to-vessel inside UT radiused section h B2.3 B-E Heater penetrations i V B2.4 B-F Nozzle-to-safe-end welds UT, S B2.5 B-G-1 Pressure-retaining bolting j B2.11 B-G-2 Pressure-retaining bolting V B2.8 B-H Integrally welded vessel supports UT B2.9 B-I-2 Vessel cladding V B2.10 B-P Exempted components i V

a. Not applicable - nozzles are cast with head and therefore UT is not feasible on inside radiused section.
b. Not applicable - supports cast with head.
c. Use shop radiographs.
d. A UT on integrally welded supports is not feasible at this time.
e. Safe-ends in branch piping welds are not applicable to North Anna.
f. There are no valve body welds at North Anna.
g. There are no integrally welded valve supports at North Anna.
h. The nozzle-to-vessel inside radiused section examination is not feasible at this time
i. IWA-5000
j. Pressure-retaining bolting (B-G-1) is not applicable to North Anna.

Revision 5209/29/2016 NAPS UFSAR 5.2-84 Figure 5.2-1 PRIMARY-SECONDARY BOUNDARY COMPONENTS SHELL LOCATIONS OF STRESS INVESTIGATIONS

Revision 5209/29/2016 NAPS UFSAR 5.2-85 Figure 5.2-2 REACTOR COOLANT PUMP CASING WITH SUPPORT FEET

Revision 5209/29/2016 NAPS UFSAR 5.2-86 Figure 5.2-3 REACTOR COOLANT PUMP SUPPORT FEET

Figure 5.2-4 REACTOR COOLANT SYSTEM WATER SOLID OPERATION Revision 5209/29/2016 NAPS UFSAR 5.2-87

Revision 5209/29/2016 NAPS UFSAR 5.2-88 Figure 5.2-5 TYPICAL REACTOR COOLANT SYSTEM HEATUP LIMITATIONS CURVE This typical heatup curve is provided for information only. As discussed in Section 5.2.3.3.1, the actual heatup curve is located in the units Technical Specifications.

Revision 5209/29/2016 NAPS UFSAR 5.2-89 Figure 5.2-6 TYPICAL REACTOR COOLANT SYSTEM COOLDOWN LIMITATIONS CURVE This typical cooldown curve is provided for information only. As discussed in Section 5.2.3.3.1, the actual cooldown curve is located in the units Technical Specifications.

Revision 5209/29/2016 NAPS UFSAR 5.2-90 This information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

Figure 5.2-7 EFFECT OF FLUENCE AND COPPER CONTENT ON SHIFT OF RTNDT FOR REACTOR VESSEL STEELS EXPOSED TO 550°F TEMPERATURE (Utilized in the development of pre-startup heatup and cooldown curves valid to 5 EFPY and 8 EFPY for Units 1 and 2 respectively.)

Revision 5209/29/2016 NAPS UFSAR 5.2-91 This information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

Figure 5.2-8 FLUENCE VERSUS FULL POWER YEARS (Utilized in the development of pre-startup heatup and cooldown curves valid to 5 EFPY and 8 EFPY for Units 1 and 2 respectively.)

Revision 5209/29/2016 NAPS UFSAR 5.2-92 Figure 5.2-9 K

ID LOWER BOUND FRACTURE TOUGHNESS A533V (REFERENCE WCAP 7623) GRADE B CLASS 1

Revision 5209/29/2016 NAPS UFSAR 5.2-93 Figure 5.2-10 CORTEN AND SAILORS CORRELATION

Figure 5.2-11 CONTAINMENT RADIATION MONITOR SENSITIVITIES Revision 5209/29/2016 NAPS UFSAR 5.2-94

Revision 5209/29/2016 NAPS UFSAR 5.3-1 5.3 THERMAL-HYDRAULIC SYSTEM DESIGN The thermal and hydraulic design bases of the reactor coolant system are described in Sections 4.3 and 4.4 in terms of core heat generation rates, DNBR, analytical models, peaking factors, and other relevant aspects of the reactor. The thermal and hydraulic characteristics are given in Tables 4.3-1, 4.4-1, 4.4-2, and 4.4-4.

Figure 5.3-1 shows a temperature-power operating map depicting Tavg as a function of percent of full power.

In order to meet the net positive suction head and seal leakage requirements for the operation of the reactor coolant pumps 1-RC-P-1A & -1B; 2-RC-P-1A, 1B, & 1C, the operating procedures state that the pressure differential across the seal must be at least 200 psi before operating the reactor coolant pump. In order to meet the net positive suction head and seal leakage requirements for the operation of the reactor coolant pump 1-RC-P-1C, the operating procedures state that the pressure differential across the No. 1 seal must be at least 200 psig before operating the reactor coolant pump.

The reactor coolant system is designed on the basis of steady-state operation at full-power heat load. The reactor coolant pumps use constant speed drives as described in Section 5.5.1. The reactor power is controlled to maintain average coolant temperature at a value that is a linear function of load, as described in Section 7.7. Transient effects are evaluated in Chapter 15 as follows: complete loss of forced reactor coolant flow (15.3.4), partial loss of forced reactor coolant flow (15.2.5), start-up of an inactive loop (15.2.6), loss of load (15.2.7), loss of normal feedwater (15.2.8), loss of offsite power (15.2.9) and accidental depressurization of the reactor coolant system (15.2.12). The natural circulation capability of the system is described in Section 15.2.9.

Revision 5209/29/2016 NAPS UFSAR 5.3-2 Figure 5.3-1 TEMPERATURE VERSUS POWER

Revision 5209/29/2016 NAPS UFSAR 5.4-1 5.4 REACTOR VESSEL AND APPURTENANCES 5.4.1 Design Bases 5.4.1.1 Codes and Specifications The vessel is Safety Class 1. The design and fabrication of the reactor vessel was in accordance with ASME Code Section III, 1968, Class A. Material specifications were in accordance with the ASME Code requirements and are given in Section 5.2.

The reactor vessel closure heads have been replaced with closure heads designed and fabricated to the French Code, RCC-M Code 1993 Edition with 1st Addenda June 1994, 2nd Addenda June 1995, 3rd Addenda June 1996, and Modification Sheets: FM 797, 798, 801, 802, 803, 804, 805, 806, and 807. The closure head sizing calculations and the stress and fatigue analysis were performed to the requirements of ASME Code Section III, 1995 Edition through 1996 Addenda. The updated Design Reports certified that the closure heads meet the design requirements and stress limits for component pressure boundaries of the ASME B&PV Code Section III, 1968 Edition through Winter 1968 Addenda.

5.4.1.2 Design Transients Cyclic loads are introduced by normal power changes, reactor trip, start-up, and shutdown operations. These design-base cycles were selected for fatigue evaluation and constitute a conservative design envelope for the projected life of the plant. Vessel analyses result in a usage factor less than one.

With regard to the thermal and pressure transients involved in the loss-of-coolant accident (LOCA), the reactor vessel was analyzed to confirm that the delivery of cold emergency core cooling water to the vessel following a LOCA would not cause a loss of integrity of the vessel.

The design specifications required analysis to prove that the vessel is in compliance with the fatigue limits of Section III of the ASME Code. The loadings and transients specified for the analysis were based on the most severe conditions expected during service. The vessel design specifications provide for design limits on heatup and cooldown rates of 100°F/hr. However, the heatup and cooldown rates imposed by plant operating limits are 50°F/hr and 75°F/hr (Reference 10) respectively. For abnormal or emergency conditions, a cooldown rate of 100°F/hr is allowed.

Design transients are discussed in detail in Section 5.2.

5.4.1.3 Protection Against Nonductile Failure Protection against nonductile failure is discussed in Section 5.2.

Revision 5209/29/2016 NAPS UFSAR 5.4-2 5.4.1.4 Inspection The internal surface of the reactor vessel can be inspected periodically using visual and/or nondestructive techniques over the accessible areas. During refueling, the vessel cladding can be inspected in certain areas between the closure flange and the primary coolant inlet nozzles, and, if deemed necessary, the core barrel can be removed, making the entire inside vessel surface accessible.

The closure head is examined visually during each refueling. Optical devices permit a selective inspection of the cladding, CRDM nozzles, and the gasket-seating surface. The knuckle transition piece, which is the area of highest stress of the closure head, is accessible on the outer surface for visual inspection, dye penetrant or magnetic particle, and ultrasonic testing. The closure studs can be inspected periodically using visual, magnetic particle, and/or ultrasonic techniques.

A control rod housing failure does not cause a propagation of failure to adjacent housings or to any other part of the reactor coolant system boundary.

The reactor vessel was designed to accommodate the requirements of the ASME Code,Section XI, Rules for Inservice Inspection of Nuclear Reactor Coolant Systems, as discussed in Section 5.2.5.

5.4.2 Description The reactor vessel is cylindrical, with a hemispherical lower head of welded construction and a removable, bolted flanged and gasketed, hemispherical upper head. The reactor vessel flange and head are sealed by two hollow metallic o-rings. Seal leakage is detected by means of two leakoff connections: one between the inner and outer ring and one outside the outer o-ring.

The vessel contains the core, core support structures, control rods, and other parts directly associated with the core. The reactor vessel closure head contains head adaptors. These head adaptors are tubular members, attached by partial penetration welds to the underside of the closure head. The upper end of these adaptors contain acme threads for the assembly of control rod drive mechanisms or instrumentation adaptors. Except for the removed part-length control rod drive mechanisms, the seal arrangement at the upper end of these adaptors consists of a welded flexible canopy seal. Due to a known generic canopy seal weld design problem that may result in canopy seal weld leakage, non-welded mechanical clamps have been installed where required to prevent canopy seal weld leakage. This clamp assembly has been specially designed by the original NSSS supplier and uses graphite sealing members to seal any canopy seal weld leakage.

The removed part-length control rod drive mechanisms were replaced with threaded caps and are seal welded with a fillet type weld. Inlet and outlet nozzles are spaced around the vessel. Outlet nozzles are located on the vessel to facilitate optimum layout of the reactor coolant system equipment. The inlet nozzles are tapered from the coolant loop vessel interfaces to the vessel inside wall to reduce loop pressure drop. Figure 5.4-1 shows the general outline and major dimensions of the vessel.

Revision 5209/29/2016 NAPS UFSAR 5.4-3 The bottom head of the vessel contains penetration nozzles for the connection and entry of the nuclear incore instrumentation. Each nozzle consists of a tubular member made of an Inconel-stainless steel composite tube. Each tube is attached to the inside of the bottom head by a partial penetration weld.

Internal surfaces of the vessel that are in contact with primary coolant have a weld overlay of at least 0.125 inch of stainless steel or Inconel. The exterior of the reactor vessel is insulated with canned stainless steel reflective sheets. The insulation is 3 inches thick and contoured to enclose the top, sides, and bottom of the vessel. All the insulation modules are removable, but access to vessel side insulation is limited by the surrounding concrete.

5.4.2.1 Fabrication Processes

1. The use of severely sensitized stainless steel as a pressure boundary material has been prohibited and has been eliminated by either a select choice of material or by programming the method of assembly (see Section 5.4.3.1). This restriction on the use of sensitized stainless steel has been established to provide the primary system with preferential materials suitable for the following:
a. Improved resistance to contaminants during shop fabrication, shipment, construction, and operation.
b. Application in critical areas.
2. Minimum preheat requirements have been established for pressure boundary welds using low-alloy weld material. Special preheat requirements have been added for stainless steel cladding of low-stressed areas. Preheat must be maintained until post-weld heat treatment, except for overlay cladding, where it may be lowered to ambient temperature under restrictive conditions. Limitations on preheat requirements are precautionary measures to decrease the probabilities of weld cracking by decreasing temperature gradients, lowering susceptibility to brittle transformation, prevention of hydrogen embrittlement, and reduction in peak hardness. Limitations on pretest requirements are precautionary measures taken to decrease temperature gradients and ensure upper transformation products on cooling along with reduction in peak hardness.
3. The CRDM head adaptor threads and surfaces of the guide studs are chrome plated to prevent possible galling of the mated parts.
4. At all locations in the reactor vessel where stainless steel and Inconel are joined, the final joining beads are Inconel weld metal to prevent cracking.
5. Specific welding process and heat treatment are as follows:
a. Base material specification and type: The base material of all nozzles in the North Anna Unit 2 reactor vessel is ASTM A-508, Class 2.

Revision 5209/29/2016 NAPS UFSAR 5.4-4

b. Process type, electrode sizes: Single-layer clad using automatic metal inert gas welding with cold wire addition and oscillation, tow-wire process using 1/16-inch-diameter wire.
c. Heat input for each layer: 230 to 290A; 34 +/-2V; 4.3 inches/minute speed.
d. Preheat, postheat, interpass temperature: Preheat temperature is 120°C (250°F) minimum; postheat temperature is preheat temperature raised to 205°C (400°F), held for 2 hours2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br />, and cooled to ambient (soaking heat treatment); interpass temperature is 200°C (392°F) maximum.
e. Postweld heat treatment (PWHT): Intermediate PWHT is 1100°F to 1175°F held for 15 minutes; final PWHT is 1100°F to 1175°F held for 1 hour/inch weld thickness.
f. Stress relief heat treatment is the same as shown in response to item (e) above.
g. Manufacturer and subcontractors: The reactor vessel was manufactured by Rotterdam Dockyard Company, Rotterdam, The Netherlands; the nozzles were clad by Sulzer Brothers Limited, Winterthur, Switzerland, as subcontractor to Rotterdam.

Principal design parameters of the reactor vessel are given in Table 5.4-1.

5.4.3 Evaluation 5.4.3.1 Steady-State Stresses Evaluation of steady-state stresses is discussed in Section 5.2.

5.4.3.2 Fatigue Analysis Based on Transient Stresses Fatigue analysis of transient stresses is discussed in Section 5.2.

5.4.3.3 Thermal Stresses Due to Gamma Heating The stresses due to gamma heating in the vessel wall were calculated by the vessel vendor and combined with the other design stresses. They are compared with the code allowable limit for mechanical plus thermal stress intensities to verify that they are acceptable. The gamma stresses are low and thus have a negligible effect on the stress intensity in the vessel.

5.4.3.4 Thermal Stresses Due to a LOCA A fracture mechanics evaluation of the reactor vessel as a result of thermal stresses following a LOCA is discussed in Section 5.2.

5.4.3.5 Heatup and Cooldown Heatup and cooldown requirements for the reactor vessel material are discussed in Section 5.2.

Revision 5209/29/2016 NAPS UFSAR 5.4-5 5.4.3.6 Irradiation Surveillance Program In the surveillance programs, the evaluation of the radiation damage is based on preirradiation testing of Charpy V-notch and tensile specimens and postirradiation testing of Charpy V-notch and tensile test specimens. Wedge-opening loading (WOL) fracture mechanics test specimens are also irradiated for potential supplemental testing. These programs are directed toward the evaluation of the effect of radiation on the fracture toughness of reactor vessel steels, based on the transition temperature approach and the fracture mechanics approach, and are in accordance with ASTM-E-185, Recommended Practice for Surveillance Tests for Nuclear Reactor Vessels (Reference 1). The North Anna units are licensed to ASTM E-185-1968. (Later editions may be used, but including only those editions through 1982. See References 7 & 11.)

The surveillance program does not include thermal control specimens. These specimens are not required, since the surveillance specimens will be exposed to the combined neutron irradiation and temperature effects and the test results will provide the maximum transition temperature shift.

Thermal control specimens as considered in ASTM-E-185 (Reference 1) would not provide any additional information on which the operational limits for the reactor vessel are set. The surveillance program will not include correlation monitors. Correlation monitors were used in the past because of inadequate neutron dosimeters. Present neutron dosimeters included in the capsules can be used to measure exposure throughout the life of the reactor vessel.

The reactor vessel surveillance program uses eight specimen capsules, more than the minimum number recommended by ASTM-E-185 (Reference 1). The capsules are located in guide baskets welded to the outside of the thermal shield, as shown in Figure 5.4-3, about 3 inches from the vessel wall directly opposite the center portion of the core. Sketches of an elevation and plan view showing the location and dimensional spacing of the capsules with relation to the core, thermal shield, and vessel and weld seams are shown in Figures 5.4-4 and 5.4-5, respectively. The capsules can be removed and replaced when the vessel head and upper internals are removed. The capsules contain SA-508 Class 2 reactor vessel forging specimens from the Unit 1 lower shell forging and the Unit 2 intermediate shell forging. The forging specimens were machined in both the tangential orientation (longitudinal axis of specimen parallel to major working direction) and axial orientation (longitudinal axis of specimen perpendicular to major working direction). The surveillance capsules also include specimens that represent the weld metal and heat-affected zone metal associated with the surveillance forgings. (As part of the surveillance program, a report of the residual elements in weight percent to the nearest 0.01% will be made for surveillance material base metal and as deposited weld metal.) The eight capsules contain 32 tensile specimens, 352 Charpy V-notch specimens (which include weld metal and heat-affected zone material), and 32 WOL specimens. Dosimeters including Ni, Cu, Fe, Co-Al, Cd shielded Co-Al, Cd shielded Np-237, and Cd shielded U-238 are placed in filter blocks drilled to contain the dosimeters. The dosimeters permit an evaluation of the flux seen by the specimens and vessel wall. In addition, thermal monitors made of low-melting alloys are included to monitor maximum

Revision 5209/29/2016 NAPS UFSAR 5.4-6 temperature of the specimens. The specimens are enclosed in a tight-fitting stainless steel sheath to prevent corrosion and ensure good thermal conductivity.

The complete capsule is helium leak tested. Vessel material sufficient for at least two capsules will be kept in storage should the need arise for additional replacement test capsules in the program. This requirement is satisfied by additional vessel surveillance material that is available from several standby surveillance capsules in each unit, and from the reactor system supplier should the need arise for additional reactor vessel material testing.

Each of four capsules (S, V, W, and Z) will contain the following specimens:

Number of Charpy Number of Tensile Number of WOL Material Specimens Specimens Specimens Limiting forging1 8 - -

Limiting forging2 12 2 4 Weld metal 12 2 -

Heat-affected zone metal 12 - -

Each of four additional capsules (T, U, X, and Y) will contain the following specimens:

Number of Charpy Number of Tensile Number of WOL Material Specimens Specimens Specimens Limiting forging1 8 - -

Limiting forging2 12 2 -

Weld metal 12 2 4 Heat-affected zone metal 12 - -

The following dosimeters and thermal monitors are included in each capsule:

Dosimeters Pure Cu Pure Fe Pure Ni Co-Al (0.15% Co)

Co-Al (Cadmium shielded)

U-238 (Cadmium shielded)

Np-237 (Cadmium shielded)

1. Specimens oriented in the major working direction (Tangential).
2. Specimens oriented normal to the major working direction (Axial).

Thermal Monitors

Revision 5209/29/2016 NAPS UFSAR 5.4-7 97.5 Pb, 2.5 Ag (579°F melting point) 97.5 Pb, 1.75 Ag, 0.75 Sn (590°F melting point)

Specimen capsules will be removed from the reactor only during normal refueling periods.

Because three of the capsules (S, T, and Z) were originally located in areas where the lead factor is less than one, capsule reinsertions from these locations to areas exceeding a lead factor of one are in the capsule withdrawal schedule. The reinsertion of the capsules with low lead factors ensures that, at the time of removal, the capsules will have received a neutron fluence greater than the maximum fluence at the vessel wall. Therefore, there will be at least one capsule leading the vessel fluence throughout the life of the vessel.

Each specimen capsule required to satisfy ASTM E-185, Conducting Surveillance Tests for Light-Water Cooled Nuclear Power Reactor Vessels, is removed after radiation exposure and transferred to a post-irradiation test facility for capsule disassembly and specimen testing.

Irradiated surveillance capsules which do not require testing to satisfy ASTM E-185 are designated as standby capsules. There currently is no detailed regulatory guidance regarding the treatment of standby capsules that are removed but not tested. To address this concern, all surveillance capsules placed in storage will be maintained for possible future insertion. If one or more capsules will not be maintained in such a way as to permit future insertion, then the NRC staff will be notified of this change (Reference 11).

The schedule for the removal and reinsertion of the capsules is shown on Tables 5.4-2 (Unit 1) and 5.4-3 (Unit 2).

5.4.3.6.1 Neutron Dosimetry Fluence data are required to (1) provide a correlation between radiation-induced property changes and fluence for surveillance specimens, and (2) determine exposure and, hence, embrittlement of the pressure vessel at the limiting weld and base metal locations. Passive dosimeters included in each surveillance capsule provide a benchmark for the determination of the neutron fluence to each surveillance capsule.

Cs-137, which has a half-life of approximately 30 years, is produced by the fission of Np-237 and U-238 dosimeters with approximately 6% fission yield. According to Draft Regulatory Guide DG-1053 (Calculation and Dosimetry Methods for Determining Pressure Vessel Neutron Fluence, dated June 1996), the nominal threshold for neutron capture resulting in fission is 0.6 MeV for Np-237 and 1.5 MeV for U-238, making the fission dosimeters most suitable for benchmarking the fast neutron fluence (E >1.0 MeV).

Dosimeters that produce short-lived isotopes provide neutron fluence benchmarks that are most representative of reactor conditions over the latter portion of the irradiation period (i.e., the fuel cycle). Although dosimeters with high effective energy ranges are insensitive to neutrons at lower energy ranges, current fluence analysis methods are able to utilize these dosimeters to

Revision 5209/29/2016 NAPS UFSAR 5.4-8 provide useful benchmark information for determining fluence estimates, even at lower energy ranges.

The energy-dependent neutron flux is not directly available from activation detectors because the dosimeters record only the integrated effect of the neutron flux on the target material as a function of both irradiation time and neutron energy. To obtain an accurate estimate of the time-averaged neutron flux incident upon the detector, the following parameters must be known:

the operating history of the reactor, the energy response of the given detector, and the neutron spectrum at the detector location.

An acceptable method for calculating surveillance capsule and reactor vessel neutron fluence is documented in Virginia Power Topical Report VEP-NAF-3-A (Reference 8). This methodology was approved by the NRC in Reference 9. Other acceptable methodologies have been previously used to determine surveillance capsule and reactor vessel neutron fluence. The approach used in the analysis of the Units 1 and 2 surveillance capsules designated U is to calculate fast flux distributions in the capsule and the reactor vessel regions. These calculated fluxes are normalized at the capsule by comparison of measured to calculated dosimeter activities.

This normalization factor is applied to all calculated fluxes in the capsule and the vessel. Fluence is obtained by a time integration of flux over the capsule irradiation period. Long-term fluence predictions are made by adjusting flux for future fuel cycle effects and then integrating over the time period of interest.

5.4.3.6.2 Analytical Model Energy-dependent neutron fluxes at the detector locations for the Units 1 and 2 surveillance capsules designated U were determined using the DOT two-dimensional discrete ordinates code (Reference 3). The North Anna reactor is modeled from the core to the shield tank in the R-Theta geometry (based on a plan view along the core midplane and one-eighth core symmetry in the azimuthal dimension). Also included is an explicit model of the surveillance capsule at the proper location. The neutron transport analysis model includes detailed models of the reactor core and reactor vessel internals. Input parameters to the code include plant-specific power distribution data, the SAILOR 47-group, ENDF-BIV-based cross-section library (Reference 4), S6 (Unit 1) or S8 (Unit 2) angular quadrature, and P3 expansion of the scattering cross-section matrix.

The surveillance capsules extend about 18 inches above and below the core midplane. Thus, the midplane flux output from the DOT calculations in R-Theta geometry requires an axial distribution adjustment to account for axial effects.

Revision 5209/29/2016 NAPS UFSAR 5.4-9 The calculation described above provides the neutron flux as a function of energy at the detector position. These calculated data are used in the following equations to obtain the calculated activities used for comparison with the experimental values. The basic equation for the activity D (in Ci/gm) is given as follows:

Nf i -i tj -i Tf D i = -----------------------

A i 3.7 x10 4 n ( E ) ( E ) Fj ( 1 - e )e (5.4-1)

E j where:

N = Avogadros number Ai= atomic weight of target material i fi = either weight fraction of target isotope in nth material or fission yield of desired isotope n(E) = group-ageraged cross sections for material n, listed in Table D-3 (E) = group-averaged fluxes calculated by DOT analysis Fj = fraction of full power during jth time interval, tj i = decay constant of ith material tj = time interval of reactor operation Tf = decay time from end of jth interval D(measured)-

C = -------------------------------- (5.4-2)

D(calculated)

Measured activity is determined for each dosimeter using established ASTM procedures.

Counting rates, which are obtained with a multichannel Ge(Li) gamma spectrometer, are converted to specific activity at the time of removal from the reactor.

All calculated fluxes are then normalized to more closely reflect the measured specific activities of the surveillance capsule dosimetry.

5.4.3.6.3 Capsule U Analysis Results for Units 1 and 2 5.4.3.6.3.1 North Anna Unit 1 Results. Capsule U was removed from North Anna Unit 1 at the end of the sixth cycle of operation. The capsule dosimeters were evaluated and found to have a cumulative fast neutron, E > 1.0 MeV, fluence of 8.28 x 1018 n/cm2. The calculated fast neutron fluence based on actual cycle power distributions at the capsule location was 8.85 x 1018 n/cm2 which compares favorably (within 7%) with the dosimeter fluence. The peak fluence at the inside surface of the reactor vessel was calculated to be 8.83 x 1018 n/cm2, which shows that the capsule has been exposed to slightly more neutrons than the vessel (Reference 5).

Revision 5209/29/2016 NAPS UFSAR 5.4-10 The material property testing included Charpy V-notch impact testing and tension testing of several specimens located with the surveillance capsule. The Charpy tests are performed to determine the transition temperature increases at 30 ft-lb and 50 ft-lb points, and the decrease in upper shelf energy. The tensile specimens were used to determine ultimate tensile strength and yield strength. The vessel specimens within Capsule U were obtained from the same girth weld and forging materials as those used in the reactor vessel beltline (Reference 5).

The irradiated specimen test results were compared to unirradiated specimen test results.

The Charpy V-notch impact test results show the irradiation has increased the average 50 ft-lb transition temperature by 80°F to 110°F, depending on the specimen metal. Irradiation has increased the average 30 ft-lb transition temperature by 65°F to 100°F, depending on the specimen metal. The upper shelf energy (average energy absorption at full shear) results show the worst decrease to be 25 ft-lb when comparing irradiated samples to unirradiated samples. The lowest average upper shelf energy was determined to be 92 ft-lb, which is greater than the 10 CFR 50 Appendix G low limit of 50 ft-lb. The Charpy impact test results from Capsule U were also satisfactorily compared to the Capsule V results. Tension test results show a slight increase in the ultimate tensile strength and the yield strength due to irradiation. Reference 5 should be consulted for specific test results.

5.4.3.6.3.2 North Anna Unit 2 Results. Capsule U was removed from North Anna Unit 2 at the end of the sixth cycle of operation. The capsule dosimeters were evaluated and found to have a cumulative fast neutron, E > 1.0 MeV, fluence of 9.55 x 1018 n/cm2. The calculated fast neutron fluence based on actual cycle power distributions at the capsule location was 1.06 x 1019 n/cm2, which compares favorably (within 11%) with the dosimeter fluence. The peak fluence at the inside surface of the reactor vessel was calculated to be 8.02 x 1018 n/cm2, which shows that the capsule has been exposed to slightly more neutrons than the vessel (Reference 6).

The material property testing included Charpy V-notch impact testing and tension testing of several specimens located with the surveillance capsule. The Charpy tests are performed to determine the transition temperature increases at 30 ft-lb and 50 ft-lb points, and the decrease in upper shelf energy. The tensile specimens were used to determine ultimate tensile strength and yield strength. The vessel specimens within Capsule U were obtained from the same girth weld and forging materials as those used in the reactor vessel beltline (Reference 6).

The irradiated specimen test results were compared to unirradiated specimen test results.

The Charpy V-notch impact test results show the irradiation has increased the average 50 ft-lb transition temperature by 25°F to 55°F, depending on the specimen metal. Irradiation has increased the average 30 ft-lb transition temperature by 13°F to 60°F, depending on the specimen metal. The upper shelf energy (average energy absorption at full shear) results showed no decrease in the average upper shelf energy of the forging and weld metals when compared to unirradiated samples. Both surveillance materials exhibit a more than adequate upper shelf energy level for continued safe plant operation (Reference 6). Tension test results show a slight increase in the ultimate tensile strength and the yield strength due to irradiation. A comparison of the

Revision 5209/29/2016 NAPS UFSAR 5.4-11 30 ft-lb transition temperature increases for the Unit 2 surveillance material with predicted increases using the methods of NRC Regulatory Guide 1.99, Revision 2, demonstrated that forging and weld material transition temperature increases were less than predicted. Reference 6 should be consulted for specific test results.

Surveillance capsule analysis results for surveillance capsules other than Capsule U are available in the various surveillance capsule analysis reports. These reports are routinely submitted to the NRC in accordance with 10 CFR 50, Appendix H.

This information was provided as part of North Annas initial license application. The units operating license does not specifically permit annealing the reactor vessel. The information contained in this section is being maintained for informational purposes only.

5.4.3.7 Capability for Annealing the Reactor Vessel There are no special design features that would prohibit the in-place annealing of the vessel. If the unlikely need for an annealing operation were required to restore the properties of the vessel material opposite the reactor core because of neutron irradiation damage, a metal temperature of approximately 750°F maximum for a maximum period of 168 hours0.00194 days <br />0.0467 hours <br />2.777778e-4 weeks <br />6.3924e-5 months <br /> would be applied. This annealing operation would be performed with the use of a special electrical space heater assembly designed to raise the affected vessel area to the required temperature for the necessary holding period. This heater assembly would consist of an insulated vessel cover assembly below which is suspended the required space heaters positioned opposite the affected area of the reactor vessel shell. The heater assembly would contain provisions for sealing to the vessel flange and waterproof electric connections. Hydraulic connections for emptying the reactor vessel of water after the assembly is in place are also required. A thermocouple assembly to monitor vessel metal temperature during annealing would also be included.

The reactor vessel materials surveillance program is adequate to accommodate the annealing of the reactor vessel. The remaining surveillance capsules at the time of annealing would be removed and given a thermal cycle equivalent to the annealing cycle. They would then be reinserted in their normal position between the core internals assembly and the reactor vessel wall. Subsequent testing of the fracture toughness specimens from the capsules would then reflect both the radiation environment before any annealing operation and after any annealing operation.

5.4.4 Tests and Inspections The reactor vessel quality assurance program is given in Table 5.4-4.

Revision 5209/29/2016 NAPS UFSAR 5.4-12 5.4.4.1 Ultrasonic Examinations

1. During fabrication, angle-beam inspection of 100% of plate material is performed to detect discontinuities that may be undetected by longitudinal wave examination, in addition to the design code straight-beam ultrasonic test.
2. The reactor vessel is examined after shop hydrotesting to provide a baseline map for use as a reference document in relation to later inservice inspections.

5.4.4.2 Penetrant Examinations The partial penetration welds for the CRDM nozzles to head are inspected by dye penetrant and on completion of welding by Ultrasonic testing methods. Bottom instrumentation tubes are inspected by dye penetrant after each layer of weld metal. Core support block attachment welds are inspected by dye penetrant after the first layer of weld metal and after each 0.5 inch of weld metal. This is required to detect cracks or other defects, lower the weld surface temperatures, improve cleanliness, and prevent microfissures.

The lifting lugs are dye penetrant tested at the conclusion of the attachment welding process.

5.4.4.3 Magnetic Particle Examinations

1. All surfaces of quenched and tempered materials are inspected on the inside diameter before cladding and on the outside diameter after hydrotesting.
2. The attachment welds for the vessel supports, lifting lugs, and refueling seal ledge are inspected after the first layer of weld metal and after each 0.5 inch of weld thickness. Where welds are backchipped, the areas are inspected before welding.

5.4.4.4 Inservice Inspection The full-penetration welds in the following areas of the installed irradiated reactor vessel are available for visual and/or nondestructive inspection, as required by ASME Code,Section XI, and described in detail in Section 5.2.5.

1. Vessel shell - the inside surface.
2. Primary coolant nozzles - the inside surface.
3. Closure head - the inside and outside surface; bottom head - the outside surface.
4. Closure studs, nuts, and washers.
5. Field welds between the reactor vessel nozzles and the main coolant piping.
6. Vessel flange seal surface.

Revision 5209/29/2016 NAPS UFSAR 5.4-13

5.4 REFERENCES

1. Standard Practice for Conducting Surveillance Tests for Light Water Cooled Nuclear Power Reactor Vessels, ASTM-E-185-68,-70,-73, -77,-82.
2. A. L. Lowe, Jr., Reactor Pressure Vessel and Surveillance Program Materials Licensing Information for North Anna Units 1 and 2, BAW-1911, Rev. 1, August 1986.
3. DOT 3.5 - Two-Dimensional Discrete Ordinates Radiation Transport Code, (CCC-276), Oak Ridge National Laboratory, WANL-TME-1982, December 1969.
4. Radiation Shielding Information Center, Oak Ridge National Laboratory, DLC-76, SAILOR Coupled Self-Shielded, 47 Neutron, 20 Gamma-Ray, P3, Cross Section Library for Light Water Reactors, March 3, 1983.
5. S. E. Yanichko and S. L. Albertin: Analysis of Capsule U from the Virginia Electric and Power Company North Anna Unit 1 Reactor Vessel Radiation Surveillance Program, WCAP-11777, dated February 1988.
6. E. Terek and S. L. Albertin: Analysis of Capsule U from the Virginia Electric and Power Company North Anna Unit 2 Reactor Vessel Radiation Surveillance Program, WCAP-12497, dated January 1990.
7. Letter from USNRC to J. P. OHanlon, North Anna Power Station, Unit 1 and Unit 2Revision to Reactor Vessel Surveillance Capsule Withdrawal Schedule, Serial No.99-446, dated August 13, 1999.
8. Virginia Power Topical Report VEP-NAF-3-A, Reactor Vessel Fluence Analysis Methodology, dated November 1997.
9. Letter from N. Kalyanam (USNRC) to J. P. OHanlon (Virginia Power), North Anna Power Station, Units 1 and 2, and Surry Power Station, Units 1 and 2Reactor Vessel Fluence Analysis Methodology (Generic Letter 92-01, Revision 1, Supplement 1) (TAC Nos. MA0555, MA0556, MA0576, and MA0577), dated April 13, 1999.
10. Letter from W.R. Matthews to USNRC, Virginia Electric and Power Company, North Anna Power Station Units 1 and 2, Proposed Technical Specifications Change Request, Reactor Coolant System Pressure/Temperature Limits, LTOPS Setpoints and LTOPS Enable Temperatures, Serial No.04-380, dated July 1, 2004.
11. Letter from E.C. Marinos USNRC to D.A. Christian (Virginia Power), North Anna Power Station, Unit Nos. 1 and 2 (North Anna 1 and 2)Approval of Proposed Reactor Vessel Material Surveillance Capsule Withdrawal Schedule (TAC Nos. MC6412 and MC6413),

Serial No.06-271, dated March 15, 2006.

Revision 5209/29/2016 NAPS UFSAR 5.4-14 Table 5.4-1 REACTOR VESSEL DESIGN PARAMETERS Parameter Value Design/operating pressure 2485/2235 psig Design temperature 650°F Overall height of vessel and closure head (bottom head 42 ft. 7-3/16 in.

o.d. to top of CRDM adapter)

Thickness of insulation, minimum 3 in.

Number of reactor closure head studs 58 Diameter of reactor closure head studs 6 in.

I.d. of flange 149-9/16 in.

O.d. of flange 184 in.

I.d. at shell 157 in.

Inlet nozzle i.d. 27-1/2 in.

Outlet nozzle i.d. 29 in.

Clad thickness, minimum 1/8 Lower head thickness, minimum 5 in.

Vessel beltline thickness, best estimate 7.862 in.

Closure head thickness, minimum 6.3 in.

Key: i.d. = inside diameter o.d. = outside diameter

Revision 5209/29/2016 NAPS UFSAR 5.4-15 Table 5.4-2 SURVEILLANCE CAPSULE WITHDRAWAL SCHEDULEa FOR NORTH ANNA UNIT 1 Capsule Capsule Lead Capsule Withdrawal Insert Est. Capsule Ident. Location b Factor c Status d EFPY/Year EFPY/Year Fluence (x 1019) e V 165° 1.6 Active 1.1/1979 NA 0.263 U 65° 1.0 Active 5.9/1987 NA 0.872 W 245° 1.03 Active 14.8/1998 NA 2.052 Z 305° 0.69 Active f 16.1/2000 NA 1.48 Z 165° 1.6 Active f NA 16.1/2000 1.48 Z 165° 1.6 Active f 44.5/2030 NA 6.49 (estimated)

T 55° 0.69 Standby g 16.1/2000 NA 1.48 T 245° 1.03 Standby g NA 16.1/2000 1.48 g

T 245° 1.03 Standby NA NA 5.33 (50.3 EFPY)

Y 295° 1.03 Standby g NA NA 6.08 (50.3 EFPY)

S 45° 0.55 Standby g NA NA 3.25 (50.3 EFPY)

X 285° 1.6 Standby f,h NA NA 9.44 (50.3 EFPY)

a. Withdrawal schedule meets requirements of ASTM E-185-82, Standard Practice for Conducting Surveillance Tests for Light-Water Cooled Nuclear Power Reactor Vessels, dated July 1, 1982. Schedule established by Reference 11 (Letter from NRC as required per 10 CFR 50 App H).
b. See Figure 5.4-5 for original capsule installation locations.
c. Lead Factor is defined in ASTM E-185-82 as the ratio of the neutron flux density at the location of the specimens in a surveillance capsule to the neutron flux density at the reactor pressure vessel inside surface at the peak fluence location.
d. Capsules required to satisfy the requirements of ASTM E-185-82 during the original license period are designated Active. Capsules not required by ASTM E-185-82, but which are maintained for contingencies, including further license renewal, are designated Standby.
e. Surveillance capsule neutron fluence estimates based on fluence analysis methodology presented in VEP-NAF-3-A, Reactor Vessel Fluence Analysis Methodology, dated April 1999. Based on the assumption of a 90% capacity factor for cycles beyond Cycle 10, 50.3 EFPY corresponds to the estimated cumulative core burnup at the end of the 60-year license period.
f. Capsule X may be withdrawn at 44.5 EFPY in lieu of Capsule Z to satisfy ASTM E-185-82 fourth capsule requirement for the license period.
g. Capsules T, Y, and S are available to satisfy potential fluence monitoring requirements during the 20-year license renewal period.
h. Capsule X may be withdrawn at end of life (EOL) to provide material properties data at a fluence which exceeds that expected to be achieved at the end of the 20-year license renewal period.

Revision 5209/29/2016 NAPS UFSAR 5.4-16 Table 5.4-3 SURVEILLANCE CAPSULE WITHDRAWAL SCHEDULEa FOR NORTH ANNA UNIT 2 Capsule Capsule Lead Capsule Withdrawal Insert Est. Capsule Ident. Location b Factor c Status d EFPY/Year EFPY/Year Fluence (x 1019) e V 165° 1.66 Active 1.0/1982 NA 0.246 U 65° 1.19 Active 6.3/1989 NA 0.980 W 245° 1.19 Active 15.3/1999 NA 2.092 Z 305° 0.81 Standby f 15.3/1999 NA 1.54 Z 165° 1.66 Standby f NA 15.3/1999 1.54 Z 165° 1.66 Active g 42.8/2029 NA 6.50 (estimated)

T 55° 0.81 Standby f 15.3/1999 NA 1.54 T 65° 1.19 Standby f NA 15.3/1999 1.54 f

T 65° 1.19 Standby NA NA 6.31 (52.3 EFPY)

Y 295° 1.19 Standby f NA NA 7.03 (52.3 EFPY)

S 45° 0.65 Standby f NA NA 3.84 (52.3 EFPY)

X 285° 1.72 Standby f,h NA NA 10.17 (52.3 EFPY)

a. Withdrawal schedule meets requirements of ASTM E-185-82, Standard Practice for Conducting Surveillance Tests for Light-Water Cooled Nuclear Power Reactor Vessels, dated July 1, 1982. Schedule established by Reference 11 (Letter from NRC as required per 10 CFR 50 App H).
b. See Figure 5.4-5 for original capsule installation locations.
c. Lead Factor is defined in ASTM E-185-82 as the ratio of the neutron flux density at the location of the specimens in a surveillance capsule to the neutron flux density at the reactor pressure vessel inside surface at the peak fluence location.
d. Capsules required to satisfy the requirements of ASTM E-185-82 during the original license period are designated Active.

Capsules not required by ASTM E-185-82, but which are maintained for contingencies, including further license renewal, are designated Standby.

e. Surveillance capsule neutron fluence estimates based on fluence analysis methodology presented in VEP-NAF-3-A, Reactor Vessel Fluence Analysis Methodology, dated April 1999. Based on the assumption of a 90% capacity factor beyond Cycle 10, 52.3 EFPY corresponds to the estimated cumulative core burnup at the end of the 60-year license period.
f. Capsules T, Y, S, and X are available to satisfy potential fluence monitoring requirements during the 20-year license renewal period. Capsule X may be withdrawn at 42.8 EFPY in lieu of Capsule Z to satisfy ASTM E-185-82 fourth cap-sule requirement for the license period.
g. Withdrawal of Capsule Z at EOL satisfies ASTM E-185-82 requirement for EOL capsule, and provide material properties data at a fluence which exceeds that expected to be achieved at the end of the 20-year license renewal period.
h. Capsule X may be withdrawn at EOL to provide material properties data at a fluence which exceeds that expected to be achieved at the end of the 20-year license renewal period.

Revision 5209/29/2016 NAPS UFSAR 5.4-17 Table 5.4-4 REACTOR VESSEL QUALITY ASSURANCE PROGRAM Examination Dye Magnetic Radiographic Ultrasonic Penetrant Particle Forgings Flange Yes Yes Studs Yes Yes Instrumentation tube Yes Main nozzles Yes Yes Nozzle belt course Yes Yes Shell courses Yes Yes Plates Transition Yes Yes Top head cap Yes Yes Bottom head cap Yes Yes Weldments Main seam Yes Yes Instrumentation tubes to vessel Yes Main nozzles to vessel Yes Yes Cladding Yes Yes Nozzle safe ends Yes Yes Yes All ferritic welds after hydrotest Yes Yes All nonferritic welds after hydrotest Yes Yes Seal ledge Yes Core pad welds Yes

Revision 5209/29/2016 NAPS UFSAR 5.4-18 Table 5.4-5 REACTOR VESSEL CLOSURE HEAD QUALITY ASSURANCE PROGRAM Examination Dye Magnetic Radiographic Ultrasonic Penetrant Particle Forgings Flanges Yes Yes Head adaptors Yes Yes Head adaptor tube Yes Yes Plates Closure Head Dome Yes Weldments CRD heat adaptors connection to Yes head Head adaptors tube to forging Yes Yes Cladding Yes Yes Head lifting lugs Yes Yes

Revision 5209/29/2016 NAPS UFSAR 5.4-19 Figure 5.4-1 REACTOR VESSEL For RV closure head see Figure 5.4-2.

Figure 5.4-2 REACTOR VESSEL HEAD Revision 5209/29/2016 NAPS UFSAR For reactor vessel dimensions see Figure 5.4-1. 5.4-20

Revision 5209/29/2016 NAPS UFSAR 5.4-21 Figure 5.4-3 SPECIMEN GUIDE TO THERMAL SHIELD ATTACHMENT

Revision 5209/29/2016 NAPS UFSAR 5.4-22 Figure 5.4-4 TYPICAL SURVEILLANCE CAPSULE ELEVATION VIEW

Revision 5209/29/2016 NAPS UFSAR 5.4-23 Figure 5.4-5 SURVEILLANCE CAPSULE, PLAN VIEWa

a. This figure reflects the original installation locations of the surveillance capsules.

Revision 5209/29/2016 NAPS UFSAR 5.4-24 Intentionally Blank

Revision 5209/29/2016 NAPS UFSAR 5.5-1 5.5 COMPONENT AND SUBSYSTEM DESIGN 5.5.1 Reactor Coolant Pumps 5.5.1.1 Design Bases The reactor coolant pump ensures an adequate core cooling flow rate, and hence enough heat transfer, to maintain a DNBR greater than the applicable DNBR design limit (Section 4.4.1.1) within the parameters of operation. The required net positive suction head is less than that available by system design and operation.

Sufficient pump rotation inertia is provided by a flywheel, in conjunction with the impeller and motor assembly, to provide adequate flow during coastdown. This flow following an assumed loss of pump power provides the core with adequate cooling.

The pump is capable of operation without mechanical damage at overspeeds up to and including 125% of normal speed.

The reactor coolant pump is shown in Figure 5.5-1 and Figure 5.5-2. The reactor coolant pump design parameters are given in Table 5.5-1.

Code and material requirements are provided in Section 5.2.

5.5.1.2 Design Description The reactor coolant pump is a vertical, single-stage, centrifugal, shaft seal pump designed to pump large volumes of reactor coolant at high temperatures and pressures.

The pump consists of three areas from bottom to top; they are the hydraulics, the shaft seals, and the motor as follows:

1. The hydraulic section consists of an impeller, diffuser, casing, thermal barrier heat exchanger, lower radial bearing, bolting ring, motor stand, and pump shaft.

2a. The 1-RC-P-1A & -1B; 2-RC-P-1A, 1B, & 1C shaft seal section consists of three identical (upper, middle, and lower) mechanical face-type sealing stages. The critical parts of each stage are the rotating face ring, stationary face ring, and secondary seals. These seals are contained within the main flange and seal housing.

2b. The 1-RC-P-1C shaft seal section consists of three devices: the number 1 controlled leakage, the film riding face seal, and the number 2 and number 3 rubbing face seals. These seals are contained within the main flange and seal housing.

3. The motor section consists of a vertical solid shaft, a squirrel cage induction-type motor, an oil-lubricated double Kingsbury-type thrust bearing, two oil-lubricated radial bearings, and a flywheel.

Revision 5209/29/2016 NAPS UFSAR 5.5-2 Attached to the bottom of the pump shaft is the impeller. The reactor coolant is drawn up through the impeller and discharged through passages in the diffuser and out through the discharge nozzles in the side of the casing. Above the impeller is a thermal barrier heat exchanger that limits heat transfer between hot system water and seal injection water.

High-pressure seal injection water is introduced through the thermal barrier wall. A portion of this water flows through the seals; the remainder flows down the shaft through and around the bearing and the thermal barrier, where it acts as a buffer to prevent system water from entering the radial bearing and seal section of the unit. The water-lubricated journal-type pump bearing, mounted above the thermal barrier heat exchanger, has a self-aligning spherical seat.

The thermal barrier heat exchanger is designed to provide backup cooling in case seal injection becomes unavailable. Westinghouse notified the industry in Nuclear Safety Advisory Letter NSAL 99-005 (Reference 12), that under certain circumstances the stabilization temperature of the bearing/seal annulus after a loss of seal injection may be higher than the operating limit. Even though the RCS water is cooled in the thermal barrier heat exchanger, reheating of the water will occur as it slowly flows up along the pump shaft. The equilibrium temperature reached after loss of seal injection flow is a function of seal leakoff flow. During a loss of seal injection, with low initial seal leakage, the 1-RC-P-1A & -1B; 2-RC-P-1A, 1B, & 1C bearing and seal operating temperature may be exceeded within 1 to 2 hours2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br />. During a loss of seal injection, with low initial number 1 seal leakage, the 1-RC-P-1C bearing and seal operating temperature may be exceeded within 1 to 2 hours2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br />. This slow temperature transient provides operators time to respond to the loss of seal injection. Significant equipment damage of the 1-RC-P-1A & -1B; 2-RC-P-1A, 1B, & 1C RCP seals and leak-off line is not expected and the seal is expected to control leakage as designed. Significant equipment damage of the 1-RC-P-1C RCP seal and leak-off line is not expected and the number 1 seal is expected to control leakage as designed. Seal failure, while not postulated for this event, is bounded by the plants LOCA analysis.

The reactor coolant pump motor bearings are of conventional design. The radial bearings are the segmented-pad type, and the thrust bearings are tilting pad Kingsbury bearings. All are oil-lubricated. The lower radial bearing and the thrust bearings are submerged in oil, and the upper radial bearing is oil fed from an impeller integral with the thrust runner.

The motor is an air-cooled, Class B thermolastic epoxy insulated, squirrel cage induction motor. The rotor and stator are of standard construction and are cooled by air. Six resistance temperature detectors are located throughout the stator to sense the winding temperature. The top of the motor consists of a flywheel and an antireverse rotation device.

Each of the reactor coolant pumps is equipped for the continuous monitoring of reactor coolant pump shaft and frame vibration levels. Shaft vibration is measured by two relative shaft probes mounted on top of the pump seal housing. The probes, one in line with the pump discharge and the other perpendicular to the pump discharge, are mounted in the same horizontal plane near

Revision 5209/29/2016 NAPS UFSAR 5.5-3 the pump shaft. A third probe, known as the keyphasor probe, provides a timing measurement of the rotating shaft, which aids in balancing the pump. Frame vibration is measured by two velocity seismoprobes located 90 degrees apart in the same horizontal plane and mounted at the top of the motor support stand. Proximeters and converters convert the probe signals to linear output that is displayed on monitor meters in the control room. The monitor meters automatically indicate the highest output from the relative probes and seismoprobes; manual selection allows the monitoring of individual probes. Indicator lights display caution and danger limits of vibration and are adjustable over the full range of the motor scale.

All parts of the pump in contact with the reactor coolant are austenitic stainless steel except for seals, bearings, and special parts. Component cooling water is supplied to the two oil coolers on the pump motor, the pump thermal barrier heat exchanger, and the stator air outlet cooler.

The pump shaft, seal housing, thermal barrier, bolting ring, and motor stand can be removed from the casing as a unit without disturbing the reactor coolant piping. The flywheel is available for inspection by removing the cover.

The performance characteristics, shown in Figure 5.5-3, are common to all of the fixed-speed mixed-flow pumps, and the knee at about 45% design flow introduces no operational restrictions, since the pumps operate at full speed.

Each reactor coolant pump is fitted with continuous strip-type temperature detectors located within the pump volute insulation. Any oil spill will collect in this enclosure, and if oil ignition occurs because of high pump casing temperature, an alarm will annunciate in the main control room.

5.5.1.3 Design Evaluation 5.5.1.3.1 Pump Performance The reactor coolant pumps deliver flow at rates that equal or exceed the required flow rates.

Initial reactor coolant system tests confirmed the total delivery capability. Thus, assurance of adequate forced circulation coolant flow was provided before initial plant operation.

The reactor trip system ensures that pump operation is within the assumptions used for loss of coolant flow analyses, which also ensures that adequate core cooling is provided to permit an orderly reduction in power if flow from a reactor coolant pump is lost during operation.

An extensive test program has been conducted for several years to develop the controlled leakage shaft seal for PWR applications. Long-term tests were conducted on less than full-scale prototype seals as well as on full-size seals. Operating plants continue to demonstrate the satisfactory performance of the controlled leakage shaft seal pump design.

Revision 5209/29/2016 NAPS UFSAR 5.5-4 Flowserve Seal [1-RC-P-1A & -1B; 2-RC-P-1A, 1B, & 1C]

Failure of one or both of the first two seal stages does not necessarily limit the operation of the seal for the continuation of an operating cycle as each seal is designed to operate at full pressure. Seal life will be greatly impacted by the higher differential pressures and leakage and Controlled Bleed Off (CBO) will increase. All factors should be taken into consideration before a seal with any failed or degraded stages are continuously operated.

The abeyance seal is a last defense to a failure of all three stages. The abeyance seal is designed to seal against the pump shaft like a collar when the flow rate is in excess of 4 gpm (equivalent) steam or 30 gpm water. Once actuated, the abeyance seal provides for limited leakage at system pressure and temperature.

From a temperature standpoint, the 1-RC-P-1A & -1B; 2-RC-P-1A, 1B, & 1C pump and seal cartridge are designed to operate continuously for at least three minutes without seal injection flow. However, long term operation without seal injection may result in particulates from the RCS causing premature seal face wear.

Westinghouse Seal [1-RC-P-1C]

The support of the stationary member of the number 1 seal (seal ring) is such as to allow large deflections, both axial and tilting, while still maintaining its controlled gap relative to the seal runner. Even if all the graphite were removed from the pump bearing, the shaft could not deflect far enough to cause an opening of the controlled leakage gap. The spring-rate of the hydraulic forces associated with the maintenance of the gap is high enough to ensure that the ring follows the runner under very rapid shaft deflections.

The testing of pumps with the number 1 seal entirely removed (full reactor pressure on the number 2 seal) shows that relatively small leakage rates would be maintained for long periods of time (approximately 100 hours0.00116 days <br />0.0278 hours <br />1.653439e-4 weeks <br />3.805e-5 months <br />), even if the number 1 seal fails entirely. The plant operator is warned of this condition by the increase in number 1 seal leakoff and has time to close this line and conduct a safe plant shutdown without significant leakage of reactor coolant to the containment. Thus, it may be concluded that gross leakage from the pump does not occur, even if seals were to suffer physical damage.

The effect of loss of offsite power on the pump itself is to cause a temporary stoppage in the supply of injection flow to the pump seals and also of the cooling water for seal and bearing cooling. The emergency diesel generators are started automatically when there is a loss of offsite power so that component cooling flow is automatically restored. Seal water injection flow is also automatically restored since the charging pump does not need to be manually restarted.

5.5.1.3.2 Coastdown Capability It is important to reactor operation that the reactor coolant continues to flow for a short time after reactor trip. To provide this flow in a station blackout condition, each reactor coolant pump

Revision 5209/29/2016 NAPS UFSAR 5.5-5 is provided with a flywheel. Thus, the rotating inertia of the pump, motor, and flywheel is used during the coastdown period to continue the flow of reactor coolant. The coastdown flow transients are provided in the figures in Section 15.3.

The pump is designed for the design-basis earthquake, and the integrity of the bearings is described in Section 5.5.1.3.4. The coastdown capability of the pumps is maintained even under the most adverse case of a blackout coincident with the design-basis earthquake.

5.5.1.3.3 Flywheel Integrity The demonstration of integrity of the reactor coolant pump flywheel is discussed in Section 5.2.3.3.3.

5.5.1.3.4 Bearing Integrity The design requirements for the reactor coolant pump bearings are primarily aimed at ensuring a long life with negligible wear, so as to give accurate alignment and smooth operation over long periods of time. To this end, the surface-bearing stresses are held very low, and even under the most severe seismic transients do not begin to approach loads that cannot be carried adequately for short periods of time.

Because there are no established criteria for short-time stress-related failures in such bearings, it is not possible to make a meaningful quantification of such parameters as margins to failure and safety factors. A qualitative analysis of the bearing design, embodying such considerations, gives assurance of the adequacy of the bearing to operate without failure.

Low oil levels in the motor bearings signal an alarm in the control room. Each motor bearing contains embedded temperature detectors, and so an initiation of failure, separate from a loss of oil, is indicated and alarmed in the control room as a high bearing temperature. High bearing temperature requires the pump to be shutdown. Even if these indications are ignored, and the bearing proceeded to fail, the low melting point of Babbitt metal on the pad surfaces ensures that no sudden seizure of the bearing will occur. In this event, the motor continues to drive, as it has sufficient reserve capacity to operate even under such conditions. However, it demands excessive currents and at some stage is shut down because of high current demand.

The reactor coolant pump shaft is designed so that its critical speed is well above the operating speed.

5.5.1.3.5 Locked Rotor It may be hypothesized that the pump impeller might severely rub on a stationary member and then seize. Analysis has shown that under such conditions, assuming instantaneous seizure of the impeller, the pump shaft fails in torsion just below the coupling to the motor, disengaging the flywheel and motor from the shaft. This constitutes a loss-of-coolant flow in the loop. Following such a postulated seizure, the motor continues to run without any overspeed, and the flywheel

Revision 5209/29/2016 NAPS UFSAR 5.5-6 maintains its integrity, as it is still supported on a shaft with two bearings. Flow transients for the assumed locked rotor are provided in the figures in Section 15.4.

There are no credible sources of shaft seizure other than impeller rubs. Any seizure of the pump bearing is precluded by graphite in the bearing. Any seizure in the seals results in a shearing of the antirotation pin in the seal ring. The motor has enough power to continue pump operation even after the above occurrences. Indications of pump 1-RC-P-1A & -1B; 2-RC-P-1A, 1B, & 1C malfunction in these conditions are initially by high temperature signals from the bearing water temperature detector and excessive seal leakoff signals. Indications of pump 1-RC-P-1C malfunction in these conditions are initially by high temperature signals from the bearing water temperature detector and excessive number 1 seal leakoff signals. Following these signals, pump vibration levels are checked. Excessive vibration indicates mechanical trouble and the pump is shut down for investigation.

5.5.1.3.6 Critical Speed It is considered desirable to operate below first critical speed, and the reactor coolant pumps are designed in accordance with this philosophy. This results in a shaft design that, even under the most severe postulated transient, gives very low values of actual stress.

Both the damped and lateral natural frequencies are determined by establishing a number of shaft sections and applying weights and moments of inertia for each section bearing spring and damping data. The torsional natural frequencies are similarly determined. The lateral and torsional natural frequencies are greater than 120% and 110% of the running speed, respectively.

5.5.1.3.7 Missile Generation Each component of the pump is analyzed for missile generation. Any fragments of the motor rotor would be contained by the heavy stator. The same conclusion applies to the pump impeller because the small fragments that might be ejected would be contained by the heavy casing. The pump flywheel is discussed in Section 5.2.3.3.

5.5.1.3.8 Pump Cavitation The minimum net positive suction head required by the reactor coolant pump at running speed is approximately 170 feet of water (approximately 85 psi). In order for the controlled leakage seal to operate correctly, it is necessary to have a differential pressure of approximately 200 psi across the seal. This is taken into consideration in the operating instructions. At this differential pressure, the net positive suction head requirement is exceeded and no limitation on pump operation occurs from this source.

5.5.1.3.9 Pump Overspeed Considerations For turbine trips actuated by either the reactor trip system or the turbine protection system, the generator and reactor coolant pumps are maintained connected to the external network for 30 seconds to maintain pump speed.

Revision 5209/29/2016 NAPS UFSAR 5.5-7 An electrical fault requiring immediate trip of the generator (with resulting turbine trip) could result in an overspeed condition. The turbine control system and the turbine intercept valves limit the overspeed to less than 120%. As additional backup, the turbine protection system has a mechanical overspeed protection trip usually set at about 111%.

5.5.1.3.10 Antireverse Rotation Device Each of the reactor coolant pumps is provided with an antireverse rotation device in the motor. This device consists of 11 pawls mounted on the outside diameter of the flywheel, a serrated ratchet plate mounted on the motor frame, a spring return for the ratchet plate, and 2 shock absorbers.

After the motor has come to a stop, one pawl engages the ratchet plate and, as the motor tends to rotate in the opposite direction, the ratchet plate also rotates until stopped by the shock absorbers. The rotor remains in this position until the motor is energized again. After the motor has come up to speed, the ratchet plate is returned to its original position by the spring return.

When the motor is started, the pawls drag over the ratchet plate until the motor reaches approximately 70 rpm. At this time, centrifugal forces acting on the pawls produce enough friction to prevent the pawls from rotating, and thus hold the pawls in the elevated position until the speed falls below the above value. Considerable shop testing and plant experience with the design of these pawls have shown high reliability of operation.

5.5.1.3.11 Shaft Seal Leakage Leakage along the reactor coolant pump shaft is controlled by three shaft seals arranged in series such that reactor coolant leakage to the containment is essentially zero. Charging flow is directed to each reactor coolant pump via a seal-water injection filter. The filter design retention capability is controlled by administrative processes that provide a filter change-out strategy. The size filter installed is dependent on plant status (e.g., shutdown, startup, or normal operations) and the amount of cleanup required. It enters the pumps through the seal housing. Here the flow splits and a portion enters the reactor coolant system via the pump shaft bearing and the thermal barrier cooler cavity. On the pumps equipped with Flowserve seals, the remainder of the flow flows up the 1-RC-P-1A & -1B; 2-RC-P-1A, 1B, & 1C pump shaft (cooling the lower bearing) and leaves the pump via the shaft seal where its pressure is reduced to that of the volume control tank. On the pumps equipped with Westinghouse seals, the remainder of the flow flows up the 1-RC-P-1C pump shaft (cooling the lower bearing) and leaves the pump via the number 1 seal where its pressure is reduced to that of the volume control tank. The water from each pump seal assembly is piped to a common manifold and then via a seal water filter through a seal water heat exchanger where the temperature is reduced to about that of the volume control tank.

Revision 5209/29/2016 NAPS UFSAR 5.5-8 Westinghouse Seal [1-RC-P-1C]

Leakage past the number 1 seal provides a constant pressure on the number 2 seal and constant pressure on the number 3 seal. A standpipe is provided to ensure a backpressure of at least 7 feet of water on the number 3 seal and warn of excessive number 2 seal leakage. The first outlet from the standpipe has an orifice to permit normal number 2 seal leakage to flow to the primary drain transfer tank; excessive number 2 leakage results in a rise in the standpipe level and eventually overflow to the primary drain transfer tank via a second overflow connection.

5.5.1.3.12 Lube Oil Collection To reduce the chance of a fire caused by lube oil leakage onto hot piping, an oil collection system has been installed for each reactor coolant pump in both units. The system consists of leakproof cans under oil-bearing components that could leak, with covers to contain oil from pressurized systems and to preclude foreign material. The components from which leakage is collected are:

  • Oil lift pumps (pressurized lines).
  • Oil cooler (pressurized lines and housing).
  • Oil level indicators.
  • Oil fill and drain points.
  • Flanged connections for the lower oil reservoir.
  • Sight glasses.
  • All flanged oil bearing connections.
  • Stator Motor Cooler (2 per motor)

Leakage from these components will be collected by seven enclosures on each RCP motor.

Each of the oil collection enclosures is routed to a header with a flexible hose; the header pipe drains the oil to a tank below the enclosures. This drain tank is sized to contain the total inventory of the motor.

5.5.1.4 Tests and Inspections Pump support feet are cast integral with the casing to eliminate a weld region.

The pump design enables disassembly and removal of the pump internals for usual access to the internal surface of the pump casing.

Inservice inspection is discussed in Section 5.2.5.

The reactor coolant pump quality assurance program is given in Table 5.5-2.

Revision 5209/29/2016 NAPS UFSAR 5.5-9 The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

5.5.1.4.1 Electroslag Welding Reactor coolant pump casings fabricated by electroslag welding were qualified as follows:

1. The electroslag welding procedure employing the two- and three-wire technique was qualified in accordance with the requirements of the ASME Code, Sections III and IX, 1965, and ASME Code Case 1355 plus supplementary evaluations as requested by WNES-PWRSD. The following test specimens were removed from an 8-inch-thick and from a 12-inch-thick weldment and successfully tested for both the two-wire and the three-wire techniques, respective. They are as follows:
a. Two-wire electroslag process inch-thick weldment.

(1) Six transverse tensile bars - 750°F post-weld stress relief.

(2) Twelve guided side bend test bars.

b. Three-wire electroslag process inch-thick weldment.

(1) Six transverse tensile bars - 750°F post-weld stress relief.

(2) Seventeen side bend test bars.

(3) Twenty-one Charpy V-notch specimens.

(4) Full-section macroexamination of weld and heat-affected zone.

(5) Numerous microscopic examinations of specimens removed from the weld and heat-affected zone regions.

(6) Hardness survey across weld and heat-affected zone.

c. A separate weld test was made using the two-wire electroslag technique to evaluate the effects of a stop and restart of welding by this process. This evaluation was performed to establish proper procedures and techniques as such an occurrence was expected during production applications due to equipment malfunction, power outages, etc. The following test specimens were removed from an 8-inch-thick weldment in the stop-restart-repaired region and successfully tested. They are as follows:

(1) Two transverse tensile bars - as welded.

(2) Four guided side bend test bars.

(3) Full-section macroexamination of weld and heat-affected zone.

d. All of the weld test blocks in a, b, and c above were radiographed using a 24-MeV Betatron. The radiographic quality level as defined by ASTM E-94 obtained was between one-half of 1% and 1%. There were no discontinuities evident in any of the electroslag welds.

Revision 5209/29/2016 NAPS UFSAR 5.5-10 The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

e. The casting segments were surface conditioned for 100% radiographic and penetrant inspections. The radiographic acceptance standards were ASTM E-186 severity level two except no category D or E defectiveness was permitted for section thickness up to 4.5 inches. The penetrant acceptance standards were ASME Code,Section III, paragraph N-627, 1965.
2. The edges of the electroslag weld preparations were machined. These surfaces were penetrant inspected before welding. The acceptance standards were ASME Code,Section III, paragraph N-627, 1968.
3. The completed electroslag weld surfaces were ground flush with the casting surface. Then, the electroslag weld and adjacent base material were 100% radiographed in accordance with ASME Code Case 1355. Also, the electroslag weld surfaces and adjacent base material were penetrant inspected in accordance with ASME Code,Section III, paragraph N-627, 1968.
4. Weld metal and base metal chemical and physical analyses were determined and certified.
5. Heat treatment furnace charts were recorded and certified.

5.5.1.4.2 In-Process Control of Variables There were many variables that had to be controlled in order to maintain desired quality welds. These, together with an explanation of their relative importance, were as follows:

5.5.1.4.2.1 Heat Input Versus Output. The heat input was determined by the product of volts times current, measured by voltmeters and ammeters that were considered accurate, as they were calibrated every 30 days. During any specific weld, these meters were constantly monitored by the operators.

The ranges specified were 500 to 620A and 44 to 50V. The correct amperage variation, even though it was less than ASME Code Case 1355 allowed, was necessary for the following reasons:

1. The thickness of the weld was in most cases the reason for changes.
2. The weld gap variation during the weld cycle also required changes. For example, the procedure qualifications provided for welding thicknesses from 5 to 11 inches with two wires. The current and voltage were varied to accommodate this range.
3. Also, the weld gap was controlled by spacer blocks. These blocks were removed as the weld progressed. Each time a spacer block was removed there was the chance of the weld pinching down to as little as 1 inch or opening to perhaps as much as 1.5 inches. In either case, a change in current may have been necessary.

Revision 5209/29/2016 NAPS UFSAR 5.5-11 The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

4. The heat output was controlled by the heat sink of the section thickness and metered water flow through the water-cooled shoes. The nominal temperature of the discharged water was 100°F.

5.5.1.4.2.2 Weld Gap Configuration. As previously mentioned, the weld gap configuration was controlled by 1.25-inch spacer blocks. As these blocks were removed there was the possibility of gap variation. It was found that a variation from 1 to 1.75 inches was not detrimental to weld quality as long as the current was adjusted accordingly.

5.5.1.4.2.3 Flux Chemistry. The flux used for welding was Arcos BV-I Vertomax. This was a neutral flux whose chemistry was specified by the Arcos Corporation. The molten slag was kept at a nominal depth of 1.75 inches and may have varied in depth by plus or minus 3/8 inch without affecting the weld. This was measured by a stainless steel dipstick.

5.5.1.4.2.4 Weld Cross-Section Configuration. The higher the current or heat input and the lower the heat output, the greater the dilution of weld metal with base metal, causing a more round barrel-shaped configuration as compared to welding with less heat input and higher heat output. This cut the amount of dilution to provide a more narrow barrel-shaped configuration.

This was also a function of section thicknesses; the thinner the section, the more round the pattern that was produced.

5.5.1.4.3 Welder Qualification Welder qualification in accordance with ASME Code,Section IX, 1965, was required, using transverse side bend test specimens per Table Q.24.1.

5.5.2 Steam Generator 5.5.2.1 Design Bases Steam generator design data are given in Table 5.5-3. The design sustains transient conditions given in Section 5.2.1. Estimates of radioactivity levels expected in the secondary side of the steam generators during normal operation, and the bases for the estimates, are given in Chapter 11. The rupture of a steam generator tube is discussed in Chapter 15.

The internal moisture separation equipment is designed to ensure that moisture carryover does not exceed 0.10% by weight, for steady-state operation up to 100% of full-load steam flow, with water at the normal operating level.

The steam generator tubesheet complex meets the stress limitations and fatigue criteria specified in the ASME Code,Section III, as well as emergency condition limitations specified in Section 5.1. Codes and material requirements for the steam generator are given in Section 5.2.

Revision 5209/29/2016 NAPS UFSAR 5.5-12 The steam generator design maximizes integrity against hydrodynamic excitation and failure of the tubes for plant life.

The water chemistry in the reactor side is selected to provide the necessary boron content for reactivity control and to minimize the corrosion of reactor coolant system surfaces.

5.5.2.2 Design Description The steam generator shown in Figure 5.5-4 is a vertical shell and U-tube evaporator with integral moisture separating equipment. The reactor coolant flows through the inverted U-tubes, entering and leaving through the nozzles located in the hemispherical bottom head of the steam generator. The head is divided into inlet and outlet chambers by a vertical partition plate extending from the head to the tubesheet. Manways are provided for access to both sides of the divided head. Steam is generated on the shell side and flows upward through the moisture separators to the outlet nozzle at the top of the vessel. The unit is primarily low alloy steel. The heat-transfer tubes are thermally treated Ni-Cr-Fe Alloy UNS N06690 and the channel head divider plate is a Ni-Cr-Fe Alloy (UNS N06600 for Unit 1 and UNS NO6690 for Unit 2). The interior surfaces of the reactor coolant channel head are weld clad with austenitic stainless steel.

The primary side interior surfaces of the tubesheet are weld clad with Ni-Cr-Fe Alloy UNS N06082.

Feedwater flows from a feedring into the annulus formed by the shell and tube bundle wrapper before entering the boiler section of the steam generator. Subsequently, a water-steam mixture flows upward through the tube bundle and into the steam drum section. A set of centrifugal moisture separators, located above the tube bundle, removes most of the entrained water from the steam. Steam dryers increase the steam quality to a minimum of 99.90% (0.10%

moisture). The moisture separators recirculate water that mixes with feedwater as it passes through the annulus formed by the shell and tube bundle wrapper.

The steam drum has two flange-bolted and gasketed access openings for inspection and maintenance of the dryer vane assembly, which can be disassembled and the vanes removed through the opening.

Two 4.0-inch inspection ports located 180° apart have been machined through the steam generator shell and wrapper above the top tube support plate to provide access for visual inspection of the inner row tube U-band region.

5.5.2.3 Design Evaluation 5.5.2.3.1 Forced Convection The limiting case for heat-transfer capability is the nominal 100% design case. The steam generator effective heat-transfer coefficient is based on the coolant conditions of temperature and flow for this case, and includes a conservative allowance for tube fouling. Enough tube area is selected to ensure that the full design heat removal rate is achieved.

Revision 5209/29/2016 NAPS UFSAR 5.5-13 5.5.2.3.2 Natural-Circulation Flow The steam generators that provide a heat sink are at a higher elevation than the reactor core, which is the heat source. Thus, natural circulation of reactor coolant is ensured for the removal of decay heat.

5.5.2.3.3 Tube and Tubesheet Stress Analyses Tube and tubesheet stress analyses of the steam generator are given in Section 5.2.

Calculations confirm that the steam generator tubesheet will withstand the loading (which is quasistatic rather than a shock loading) caused by a loss of reactor coolant.

5.5.2.3.4 Corrosion In sizing components, design formulas take into account allowances for general corrosion.

These allowances are based on corrosion tests on representative materials in simulated primary and secondary side environments. Conservative design basis allowances for ferritic and stainless steels and Ni-Cr-Fe Alloy 600 are summarized in WNEP-8661, Rev. 1. Corrosion allowances established for Ni-Cr-Fe Alloy 600 provide conservative upper limits for corrosion losses in Ni-Cr-Fe Alloy 690. Corrosion tests (EPRI Report NP-6997-SD) on Alloy 690TT tubes exposed to simulated primary water coolant at 330°C for 1500 hours0.0174 days <br />0.417 hours <br />0.00248 weeks <br />5.7075e-4 months <br /> showed an average metal loss to the stream of 0.011383 mg/dm2/day, and an average total descaled metal loss 0.0425 mg/dm2/day.

The latter descaled metal loss corresponds to 0.0072 mils per year, or 0.44 mils in 60 years, which is insignificant compared to the minimum tube wall thickness. The general corrosion loss in secondary side AVT water chemistry is expected to be equally low.

Extensive corrosion testing of thermally treated Alloy 690 tubing (EPRI Report NP-6997-SD) has shown that Alloy 690 is (i) virtually immune to primary water stress corrosion cracking, (ii) extremely resistant to stress corrosion cracking in secondary side AVT water chemistry, and (iii) is resistant to secondary side faulted off-chemistry conditions.

Chemistry control of steam generator water to minimize corrosive attack on the steam generator components is discussed in Section 10.4.3.2.

5.5.2.3.5 Flow-Induced Vibration In the design of Westinghouse Model 51F steam generators used at North Anna Power, the possibility of tube degradation due to either mechanical or flow-induced excitation was considered. This evaluation included detailed analysis of the tube support systems as well as an extensive research program with tube vibration model tests.

Consideration was given to potential sources of tube excitation including primary fluid flow within the U-tubes, mechanically-induced vibration, and secondary fluid flow on the outside of the tubes. The effects of primary fluid flow and mechanically-induced vibration are considered to be negligible during normal operation. The primary source of potential tube degradation due to

Revision 5209/29/2016 NAPS UFSAR 5.5-14 vibration is the hydrodynamic excitation by the secondary fluid on the outside of the tubes, and this area has been emphasized in both analyses and tests, including evaluation of steam generator operating experience.

Three potential tube vibration mechanisms due to hydrodynamic excitation by the secondary fluid on the outside of the tubes have been identified and evaluated. These include potential flow-induced vibrations resulting from vortex shedding, turbulence, and fluidelastic vibration mechanisms.

Vortex shedding is possible, at most, only for the outer few rows in the wrapper inlet region of steam generators such as the Model 51F for which non-uniform, two-phase turbulent flow exists throughout most of the tube bundle. Moderate tube response caused by vortex shedding is observed in some carefully controlled laboratory tests on idealized tube arrays. However, no evidence of tube response caused by vortex shedding is observed in steam generator scale model tests simulating the wrapper inlet region. Bounding calculations consistent with laboratory test parameters confirmed that vibration amplitudes would be acceptably small, even if the carefully controlled laboratory conditions were unexpectedly reproduced in the steam generator.

Flow-induced vibrations due to flow turbulance are also small; root mean square amplitudes are less than allowances used in tube sizing. These vibrations cause stresses which are two orders of magnitude below fatigue limits for the tubing material. Therefore, neither unacceptable tube wear nor fatigue degradation is anticipated due to secondary flow turbulance in the Model 51F design configuration.

Fluidelastic tube vibration is potentially more severe than either vortex shedding or turbulance because it is a self-excited mechanism: relatively large tube amplitudes can feedback proportional driving forces if an instability threshold is exceeded. Tube support spacing incorporated into design of both the tube support plates and the anti-vibration bars in the U-bend region provides tube response frequencies such that the instability threshold is not exceeded for secondary fluid flow conditions. This approach provides large margins against initiation of fluidelastic vibration for tubes which are effectively supported by the Model 51F tube support configuration.

Small clearances between the tubes and supporting structure are required for steam generator fabrication. These clearances introduce the potential that any given tube support location may not be totally effective in restraining tube motion if there is a finite gap around the tube at that location. Fluidelastic tube response within available support clearances is therefore theoretically possible if secondary flow conditions exceed the instability threshold assuming no support at the location with a gap around the tube.

This potential has been investigated both with tests and analyses for the U-bend region where secondary flow conditions have the potential to exceed the instability threshold if a tube does not contact two or more sequential supports as a result of fabrication tolerances. Tube

Revision 5209/29/2016 NAPS UFSAR 5.5-15 vibration response is shown to have wear potential within available design margins even for limiting tube fitup conditions which are not expected. Corresponding tube bending stresses remain more than an order of magnitude below fatigue limits as a consequence of vibration amplitudes constrained by available clearances. These analyses and tests for limiting postulated fitup conditions include simultaneous contributions from flow turbulence.

Potential tube fatigue subject to postulated conservative tube support, material, and environmental conditions has also been evaluated to demonstrate added margin against rapidly propagating fatigue. Reduced damping, due to postulated clamped conditions at the top tube supports and at anti-vibration bars (AVBs) in the U-bend region, does not result in fluidelastic instability for small radius tubes as a result of the consistently controlled depth of AVB insertion which is deeper than that of previous operating steam generators. Postulated combinations of tube clamping and adjacent support with clearances for larger radius tubes do not lead to tube stresses above fatigue limits which have been reduced below ASME Code limits to address postulated material and environmental degradation.

Analysis and tests therefore demonstrate that unacceptable tube degradation resulting from tube vibration is not expected for the 51F steam generators at North Anna Power Station.

Operating experience with similar steam generators supports this conclusion.

5.5.2.4 Tests and Inspections The steam generator quality assurance program is given in Table 5.5-4.

Radiographic inspection and acceptance standard are in accordance with the requirements of Section III of the ASME Code, 1986.

Liquid penetrant inspection is performed on weld-deposited tubesheet cladding, channel head cladding, tube-to-tubesheet weldments, and weld-deposited cladding. Liquid-penetrant inspection and acceptance standards are in accordance with the requirements of Section III of the ASME Code, 1986.

Magnetic particle inspection is performed on the tubesheet forging, channel head forging, shell forging, nozzle forgings, and the following weldments:

1. Nozzle to shell.
2. Structural attachments.
3. Instrument connections (primary and secondary).
4. Vessel surfaces after temporary attachments removal.
5. All accessible pressure retaining welds after hydrostatic test.

Magnetic particle inspection and acceptance standards are in accordance with the requirements of Section III of the ASME Code, 1986.

Revision 5209/29/2016 NAPS UFSAR 5.5-16 An ultrasonic test is performed on the channel head and tubesheet forgings, channel head and tubesheet cladding, secondary forgings, shell and head plates, and nozzle forgings.

The heat-transfer tubing is subjected to eddy current test.

Hydrostatic tests were performed in accordance with Section III of the ASME Code, 1986.

In addition, the heat-transfer tubes are subjected to a hydrostatic test pressure, before installation into the vessel, which is not less than 1.25 times the primary-side design pressure.

Manways are provided to access both the primary and secondary sides.

The steam generator tubes are inspected in accordance with the Technical Specifications.

5.5.3 Reactor Coolant Piping 5.5.3.1 Design Bases The reactor coolant system piping is designed and fabricated to accommodate the system pressures and temperatures attained under all expected modes of plant operation or expected system interactions. Code and material requirements are provided in Section 5.2.

Materials of construction are specified to minimize corrosion/erosion and ensure compatibility with the operating environment.

The piping in the reactor coolant system pressure boundary is designed and fabricated in accordance with B31.7, 1969. However, reanalysis of the pressurizer surge line to account for the effect of thermal stratification and striping was performed in accordance with the requirements of ASME Boiler and Pressure Vessel Code,Section III, 1986 and addenda through 1987 incorporating high cycle fatigue as required by NRC Bulletin 88-11.

5.5.3.2 Design Description Principal design data for the reactor coolant piping are given in Table 5.5-5.

The reactor coolant system piping is specified in the smallest sizes consistent with system requirements. In general, high fluid velocities are used to reduce piping sizes. This design philosophy results in the reactor inlet and outlet piping diameters given in Table 5.5-5. The line between the steam generator and the pump suction is larger to reduce pressure drop and improve flow conditions to the pump suction.

The reactor coolant piping and fittings are cast. Cast sections of large 90-degree elbows are joined by electroslag welds. All materials are austenitic stainless steel. All smaller piping that comprises part of the reactor coolant system boundary, such as the pressurizer surge line, spray and relief line, loop drains, and connecting lines to other systems, are also austenitic stainless steel. The nitrogen supply line for the pressurizer relief tank is carbon steel. All joints and connections are welded, except for the pressurizer code safety valves, where flanged joints are used. Thermal sleeves were originally installed at points in the system where high thermal stresses

Revision 5209/29/2016 NAPS UFSAR 5.5-17 could develop from rapid changes in fluid temperature during normal operational transients.

These points included the following:

1. Charging connections at the primary loop from the Chemical and Volume Control System, including loop fill connections.
2. All accumulator discharge lines and the return line connections from the residual heat removal system at the reactor coolant loops.
3. Both ends of the pressurizer surge line.
4. Pressurizer spray line connection at the pressurizer.
5. Six-inch cold-leg safety injection nozzles.

The accumulator discharge lines, as noted above, are also used as the return line connections for the residual heat removal system. Because that system is expected to be in operation many times throughout the life of the plant (see Section 5.2.1) these lines were equipped with thermal sleeves to reduce the thermal stresses that could develop when the residual heat removal system is put into operation. The other ECCS injection connections are not expected to be in use during normal operation and, as such, are not expected to experience a large number of cycles of thermal stresses. Consequently, the connections are not equipped with thermal sleeves.

Some of the thermal sleeves have been removed because of weld defects discovered during operation. Details are given in Section 5.5.3.2.1 below.

All piping connections from auxiliary systems are made above the horizontal centerline of the reactor coolant piping, with the exception of the following:

1. Residual heat removal pump suction, which is 45 degrees down from the horizontal centerline. This enables the water level in the reactor coolant system to be lowered in the reactor coolant pipe while continuing to operate the residual heat removal system, should this be required for maintenance.
2. Loop drain lines and the connection for temporary measurement of water in the reactor coolant system during refueling and maintenance operation.
3. The differential-pressure taps for flow measurement are downstream of the steam generators on the first 90-degree elbow. The tap arrangement is discussed in the instrumentation section of this description.

Penetrations into the coolant flow path are limited to the following:

1. The spray line inlet connections extend into the cold-leg piping in the form of a scoop so that the velocity head of the reactor coolant loop flow adds to the spray driving force.

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2. The reactor coolant sample system taps protrude into the main stream to obtain a representative sample of the reactor coolant.
3. The resistance temperature detector hot-leg connections are scoops that extend into the reactor coolant to collect a representative temperature sample for the resistance temperature detector.
4. The wide-range temperature detectors are located in resistance temperature detector wells that extend into the reactor coolant pipes.

Three thermowell mounted resistance temperature detectors are installed in the hot leg scoops of each loop near the inlet to the steam generator for reactor protection and control. The scoops are 120 degrees apart in the cross-sectional plane of the reactor coolant leg, and extended into the pipe to sample the flow.

One thermowell mounted resistance temperature detector is installed in the cold leg nozzle of each loop at the discharge of the reactor coolant pump for reactor protection and control.

Signals from these instruments are used to compute the reactor coolant delta T (temperature of the hot leg, Thot, minus the temperature of the cold leg, Tcold) and an average reactor coolant temperature (Tavg). The Tavg for each loop is indicated on the main control board.

The reactor coolant system piping includes those sections of piping interconnecting the reactor vessel, steam generator, and reactor coolant pump. It also includes the following:

1. Charging line and alternate charging line from the isolation valve up to the branch connections on the reactor coolant loop.
2. Letdown line and excess line from the branch connections on the reactor coolant loop to the isolation valve.
3. Pressurizer spray lines from the reactor coolant cold legs to the spray nozzle on the pressurizer vessel.
4. Residual heat removal lines to or from the reactor coolant loops up to the designated isolation valve.
5. Safety injection lines from the designated isolation or check valve to the reactor coolant loops.
6. Accumulator lines from the designated isolation or check valve to the reactor coolant loops.
7. Loop fill, loop drain, sample, and instrument lines to or from the designated isolation valve to or from the reactor coolant loops.
8. Pressurizer surge line from one reactor coolant loop hot leg to the pressurizer vessel inlet nozzle.

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9. Resistance temperature detector scoop element, pressurizer spray scoop, sample connection with scoop, reactor coolant temperature element installation boss, and the temperature element well itself.
10. All branch connection nozzles attached to reactor coolant loops.
11. Pressure relief lines from nozzles on top of the pressurizer vessel up to and through the power-operated pressurizer relief valves and pressurizer safety valves.
12. Seal injection water and labyrinth differential-pressure lines to or from the reactor coolant pump inside reactor containment.
13. Auxiliary spray line from the isolation valve to the pressurizer spray line headers.
14. Sample lines from pressurizer to the isolation valve.
15. Loop bypass lines.

Details of the materials of construction and codes used in the fabrication of reactor coolant piping and fittings are discussed in Section 5.2.

5.5.3.2.1 Thermal Sleeve Modification During an investigation of the thermal sleeves located in the nozzles to the reactor coolant loops, it was discovered that, in some cases, the welds that attach the thermal sleeves to the inside of the respective nozzles were not intact. The loss of the welds creates the potential for the sleeves to slide down or fall into the loop piping. The affected thermal sleeves for Units 1 and 2 are shown in Table 5.5-6. The resolution of this problem was to remove from the reactor coolant system piping the thermal sleeves identified in Table 5.5-6. The piping sections for the nozzles in the Unit 1, 3-inch charging line, 12-inch accumulator line, and the four Unit 2 lines listed in Table 5.5-6 were cut away to remove the thermal sleeves, and were welded back in place after the inside of the nozzle was examined for surface damage, repaired as necessary, and wall thickness verified. The thermal sleeve in the 6-inch Loop 1 cold leg safety injection line had become loose and was retrieved from the reactor coolant system.

Since both units continue operating with the rest of similar design sleeves in place, detailed evaluations on the safety aspects of operation with affected thermal sleeves were performed and submitted to the NRC (References 1 & 2) for Units 1 and 2 respectively. In addition, VEPCO initiated a program of increased operator training and awareness to address the concerns of loose parts in the reactor coolant system. Reference 2 provides a description of this program.

5.5.3.3 Design Evaluation Piping load and stress evaluation for normal operating loads, seismic loads, blowdown loads, and combined normal, blowdown, and seismic loads are discussed in Section 5.2.

Revision 5209/29/2016 NAPS UFSAR 5.5-20 5.5.3.3.1 Material Corrosion/Erosion Evaluation An upper limit of about 50 ft/sec is specified for internal coolant velocity to avoid the possibility of accelerated erosion. All pressure-containing welds out to the second valve that delineates the reactor coolant pressure boundary (RCPB) are available for examination with removable insulation.

Components with stainless steel will operate satisfactorily under normal plant chemistry conditions in PWR systems, because chlorides, fluorides, and particularly oxygen, are controlled to very low levels.

Periodic analysis of the coolant chemical composition is performed to monitor the adherence of the system to desired reactor coolant water quality listed in Table 5.2-25. The maintenance of the water quality to minimize corrosion is accomplished using the Chemical and Volume Control System and sampling system, which are described in Chapter 9.

5.5.3.3.2 Sensitized Stainless Steel Sensitized stainless steel is discussed in Section 5.2.3 5.5.3.3.3 Contaminant Control Contamination of stainless steel and Inconel by copper, low-melting temperature alloys, mercury, and lead is prohibited.

Before the application of thermal insulation, the surfaces of austenitic stainless steel pipe are cleaned using approved site cleaning procedures. These procedures ensure that chlorides, fluorides, and other chemical contaminants will be eliminated or reduced to very low levels where they will not affect plant safety.

5.5.3.4 Tests and Inspections The reactor coolant system piping quality assurance program is given in Table 5.5-7.

Inservice inspection is discussed in Section 5.2.5.

5.5.4 Residual Heat Removal System The residual heat removal system transfers heat from the reactor coolant system to the component cooling system to reduce the temperature of the reactor coolant to the cold shutdown temperature at a controlled rate during the latter part of normal plant cooldown and maintains this temperature until the plant is started up again.

The residual heat removal system can also be used to transfer refueling water from the refueling cavity to the refueling water storage tank following a refueling operation.

5.5.4.1 Design Bases Residual heat removal system design parameters are listed in Table 5.5-8.

Revision 5209/29/2016 NAPS UFSAR 5.5-21 The residual heat removal system is designed to remove residual heat from the core and reduce the temperature of the reactor coolant system during the second phase of plant cooldown.

During the first phase of cooldown, the temperature of the reactor coolant system is reduced by transferring heat from the reactor coolant system to the steam and power conversion system through the use of steam generators.

The residual heat removal system is placed in operation approximately 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> after reactor shutdown, when the temperature and pressure of the reactor coolant system are approximately 350°F and 450 psig. Assuming that two heat exchangers and two pumps are in service and that each heat exchanger is supplied with component cooling water at design flow and temperature, the residual heat removal system is designed to reduce the temperature of the reactor coolant from 350°F to 140°F within 16 hours1.851852e-4 days <br />0.00444 hours <br />2.645503e-5 weeks <br />6.088e-6 months <br />. The heat load handled by the residual heat removal system during the cooldown transient includes residual heat from the core and reactor coolant pump heat.

The design residual heat load is based on the residual heat fraction that exists at 20 hours2.314815e-4 days <br />0.00556 hours <br />3.306878e-5 weeks <br />7.61e-6 months <br /> following reactor shutdown from an extended run at full power.

5.5.4.2 System Description The residual heat removal system as shown in Figure 5.5-5 and Reference Drawing 4 consists of two residual heat exchangers, two residual heat removal pumps, and the associated piping, valves, and instrumentation necessary for operational control. The inlet line to the residual heat removal system is connected to the hot leg of reactor coolant loop 1, while the return lines are connected to the cold legs of the other two reactor coolant loops.

The residual heat removal system suction line is isolated from the reactor coolant system by two motor-operated valves in series while the discharge lines are isolated by a motor-operated valve in series with a check valve in each line. The residual heat removal system is located completely inside the containment.

Interlocks are not provided or required on the motor-operated valves in the RHR discharge lines to the RCS. These valves are under administrative control to be shut whenever the RCS pressure is greater than RHR design pressure. In addition, check valves are provided downstream of the motor-operated valves to provide further isolation of the RHR system from the RCS.

Periodic tests of these check valves ensure their operability.

During system operation, reactor coolant flows from the reactor coolant system to the residual heat removal pumps, through the tube side of the residual heat exchangers, and back to the reactor coolant system. The heat load is transferred in the residual heat exchangers to the component cooling water circulating through the shell side of the heat exchangers.

Coincident with reactor cooldown, heatup, or operation at cold shutdown, a portion of the reactor coolant flow may be diverted from downstream of the residual heat exchanger to the Chemical and Volume Control System low-pressure letdown line for purification and/or pressure control. By regulating the diverted flow rate and the charging flow, the reactor coolant system

Revision 5209/29/2016 NAPS UFSAR 5.5-22 pressure may be controlled. Pressure regulation is necessary to maintain the pressure range dictated by the fracture prevention criteria requirements of the reactor vessel and by the number 1 seal differential pressure and NPSH requirements of the reactor coolant pumps.

The reactor coolant system cooldown rate is manually controlled by regulating the reactor coolant flow through the tube side of the residual heat exchangers. A line, containing a flow control valve, bypasses the residual heat exchangers and is used to maintain a constant return flow to the reactor coolant system. Instrumentation is provided to monitor system pressure, temperature, and total flow.

The residual heat removal system may also be used to drain the refueling cavity after refueling. Water is pumped back to the refueling water storage tank until the water level is lowered to the flange of the reactor vessel. The remainder is removed by the refueling purification system (Section 9.1.3) via the drain connection at the bottom of the refueling canal.

When the residual heat removal system is in operation, the water chemistry is the same as that of the reactor coolant. Provision is made for the sampling system to extract samples from the flow of reactor coolant downstream of the residual heat exchangers. A sampling point is also provided between the pumps and heat exchangers.

5.5.4.2.1 Component Description The materials used to fabricate residual heat removal system components are in accordance with the applicable code requirements. All parts of components in contact with borated water are fabricated or clad with austenitic stainless steel or equivalent corrosion resistant material.

Component codes and classifications are given in Table 5.5-9 and component parameters are listed in Table 5.5-10.

5.5.4.2.1.1 Residual Heat Removal Pumps. Two pumps are installed in the residual heat removal system. The pumps are sized to deliver reactor coolant flow through the residual heat exchangers to meet the plant cooldown requirements. Two pumps ensure that cooling capacity is not lost should one pump become inoperative.

A recirculation line is provided from the heat exchanger to the pump suction to prevent pump overheating when the residual heat removal discharge MOVs are closed. A manual valve in the recirculation line is administratively locked in position to establish an adequate recirculation flow while ensuring cooling flow through the system.

A local pressure indicator is located immediately downstream of each residual heat removal pump to indicate the pump discharge pressure. A local pressure indicator is also located in the common discharge header downstream of the residual heat pumps to indicate the heat exchanger inlet pressure and to provide a high-pressure alarm to the annunciator located on the main control board.

Revision 5209/29/2016 NAPS UFSAR 5.5-23 The two pumps are vertical, centrifugal units with mechanical shaft seals. All pump surfaces in contact with reactor coolant are austenitic stainless steel or equivalent corrosion-resistant material.

5.5.4.2.1.2 Residual Heat Exchangers. Two residual heat exchangers are installed in the system.

The heat exchanger design is based on heat load and temperature differences between reactor coolant and component cooling water existing 20 hours2.314815e-4 days <br />0.00556 hours <br />3.306878e-5 weeks <br />7.61e-6 months <br /> after reactor shutdown, when the temperature difference between the two systems is small.

The installation of two heat exchangers ensures that the heat removal capacity of the system is only partially lost if one heat exchanger becomes inoperative.

The residual heat exchangers are of the shell and U-tube type. Reactor coolant circulates through the tubes, while component cooling water circulates through the shell. The tubes are welded to the tubesheet to prevent leakage of reactor coolant.

5.5.4.2.1.3 Residual Heat Removal System Valves. Valves that perform a modulating function are equipped with two sets of packings and an intermediate leakoff connection that discharges to the drain header.

Manual and motor-operated valves have backseats to facilitate repacking and to limit stem leakage when the valves are open. Leakage connections are provided where required by valve size and fluid conditions.

As shown in Table 5.5-10, the design flow of the residual heat removal suction relief valves is 900 gpm. As installed, each valve can flow approximately 700 gpm. This installed capacity is in excess of the maximum expected charging flow for a charging/letdown mismatch event, and therefore adequate to protect the residual heat removal system from overpressurization.

5.5.4.2.2 System Operation 5.5.4.2.2.1 Reactor Start-up. Start-up encompasses the operations that bring the reactor from cold shutdown to no-load operating temperature and pressure. Generally, while at cold shutdown condition, residual heat from the reactor core is being removed by the residual heat removal system. Flow through the heat exchangers is adjusted in response to the residual heat removal load at the time.

At initiation of the plant start-up, the reactor coolant system is completely filled, and the pressurizer heaters are energized. Pressure control is achieved by balancing makeup flow to the coolant system with flow from the residual heat removal connection to letdown. This line taps off from the common header downstream of the residual heat exchanger. The failure of any of the valves in the line from the residual heat removal system to the Chemical and Volume Control System has no safety implications, either during start-up or cooldown.

Revision 5209/29/2016 NAPS UFSAR 5.5-24 After the first reactor coolant pump is started, a pressurizer steam bubble is formed, and the residual heat removal pumps are stopped. The indication of steam bubble formation is provided in the main control room by the damping out of the reactor coolant system pressure fluctuations and by pressurizer level indication. The residual heat removal system is then isolated from the reactor coolant system and the system pressure is controlled by normal letdown and the pressurizer spray and pressurizer heaters. The remaining reactor coolant pumps are started as necessary.

5.5.4.2.2.2 Power Generation and Hot Standby Operation. During power generation and hot standby operation, the residual heat removal system is not in service. The RHR to letdown interface valve is maintained slightly open during normal operations in order to keep RHR water solid, and allow for RHR expansion and contraction due to temperature changes.

5.5.4.2.2.3 Plant Shutdown. Plant shutdown encompasses the operations that bring the reactor from hot no-load temperature and pressure to cold shutdown conditions.

The initial phase of reactor cooldown is accomplished by transferring heat from the reactor coolant system to the steam and power conversion system through the use of the steam generators.

When the reactor coolant temperature and pressure are reduced to approximately 350°F and 450 psig, approximately 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> after reactor shutdown, the second phase of cooldown starts with the residual heat removal system being place in operation.

The start-up of the residual heat removal system includes a warm-up period during which time reactor coolant flow through the heat exchangers is limited to minimize thermal shock. The rate of heat removal from the reactor coolant is manually controlled by regulating the coolant flow through the residual heat exchangers. By adjusting the control valve downstream of the residual heat exchangers, the mixed mean temperature of the return flow is controlled.

Coincident with the manual adjustment, the heat exchangers bypass valve is regulated to give the required total flow.

The reactor cooldown rate is limited by reactor coolant system equipment cooling rates based on allowable stress limits, as well as the operating temperature limits of the component cooling system. As the reactor coolant temperature decreases, the reactor coolant flow through the residual heat exchangers is increased.

The residual heat removal system is designed to reduce the temperature of the reactor coolant from 350°F to 140°F over a period of 16 hours1.851852e-4 days <br />0.00444 hours <br />2.645503e-5 weeks <br />6.088e-6 months <br />. If one residual heat removal system heat exchanger is not operable, the cooldown time will increase. This increased cooldown time does not adversely affect the safe operation of the reactor.

The residual heat removal system is operated with only one pump in service. In this configuration, cooldown from 350°F to 200°F can be achieved in less than 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />, which meets the Technical Specification requirements for a forced cooldown. After the reactor coolant

Revision 5209/29/2016 NAPS UFSAR 5.5-25 pressure is reduced and the temperature is 140°F or lower, the reactor coolant system may be opened for refueling or maintenance.

5.5.4.2.2.4 Refueling. During refueling, the residual heat removal system is maintained in service with the number of pumps and heat exchangers in operation as required by the heat load.

Following refueling, the residual heat removal pumps may be used to drain the refueling cavity to the top of the reactor vessel flange by pumping water from the reactor coolant system to the refueling water storage tank.

5.5.4.2.2.5 Monitoring Instrumentation. Information displayed in the control room to monitor the adequacy of cooling and lubrication of RHR pumps includes the following:

1. Visual and audio alarms for low cooling water flow to the residual heat removal pumps.
2. Residual heat removal pump seal water cooler outlet temperature is provided to the control room computer.

5.5.4.3 Design Evaluation 5.5.4.3.1 System Availability and Reliability The system is provided with two residual heat removal pumps and two residual heat exchangers. If one of the two pumps or one of the two heat exchangers is not operable, safe cooldown of the plant is not compromised; however, the time required for cooldown is extended.

To ensure reliability, the two residual heat removal pumps are connected to two separate electrical buses so that each pump receives power from a different source. If a total loss of offsite power occurs while the system is in service, each bus has the capability of being manually transferred to a separate emergency diesel power supply.

For Unit 1, there is a 6-foot separation between the residual heat removal pumps and an 18.5-foot separation between the residual heat removal heat exchangers. For Unit 2, the distance between the pumps is 16 feet 5 inches, and the distance between the heat exchangers is 19 feet 6 inches. There is no flammable material in the area of the pumps, other than the oil in the motors, so the loss of both pumps in a fire is not credible. To satisfy 10 CFR 50 Appendix R requirements, a radiant energy shield is installed in both units between the residual heat pump motors. The main components of the residual heat removal system are located on a separate mezzanine with adequate drainage so that any flooding from a pipe rupture will not collect in the area of the system. The residual heat removal system is located in a separate area not subject to missiles, pipe whip, or jet impingement from high-energy lines. Therefore, the system, because of separation and adequate protection from common hazards, would not be incapacitated.

Should one residual heat removal pump shaft seal fail, there will be no adverse effects on the other pump. The pumps are mounted vertically. Should shaft seal failure occur, gross leakage along the shaft is prevented by a throttle bushing atop the seal. Any water that might work up

Revision 5209/29/2016 NAPS UFSAR 5.5-26 along the shaft will be directed upward against the bottom face of the pump motor and redirected downward. Because the air intakes of the motors are at the top of the motors, the leaking water would not rise this high after hitting the underside of the motor on the leaking pump. These are the only seals in this vicinity. The capacity of the containment sump pumps is 25 gpm each.

The occurrence of a break in a residual heat removal line during a normal shutdown or heatup when in the residual heat removal mode of operation is considered highly unlikely. For example, the reactor coolant system pressure in that mode would be 450 psig compared to the residual heat removal design pressure of 600 psig. However, such an event has been analyzed for a postulated residual heat removal moderate energy line break during shutdown. The analysis is conservatively based on the break occurring within 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> after reactor shutdown, the reactor coolant system at 450 psig and 350°F, and the pressurizer level at 21.4%. An assessment was also made to determine the equipment necessary to mitigate a residual heat removal line break to ensure that the core is again covered.

The analysis showed that the operator has 44 minutes after the initial alarm to take any appropriate action to ensure core immersion. The analysis further established that (1) one charging/safety injection pump will provide adequate flow to sustain the system in a safe condition and (2) an initial alarm signal low-pressurizer-level deviation alarm conservatively assumed at 16.4% will occur within 30 seconds of the event initiation, followed by another alarm (low-level heater cutoff) at 15%. The analysis conservatively assessed the largest residual heat removal line that could adversely impact both residual heat removal trains simultaneously. The break area was developed consistent with moderate energy line break criteria and was established to be 0.008 ft2. Results of the analysis confirm that the required makeup can be provided by the inservice charging/safety injection pump. Even if (1) a 10-minute delay time for operator action and (2) a single failure were assumed, they would not result in an unsafe condition. Specifically, 34 minutes should still remain available for the initiation and effective operation of necessary equipment. Moreover, it is only if the single-failure assumption is invoked that operator action to start the backup charging/safety injection pump would be necessary. The operator can initiate the starting of the pump from within the main control room and flow can be established within 1 minute. Primary coolant loss through the break will lower the level in the reactor vessel to the hot-leg nozzle elevation, assuming no charging/safety injection pump flow, at 33 minutes from break initiation. The start of charging/safety injection pump flow in 11 minutes will delay that time, and the level will stabilize at the hot-leg nozzle level until the break is isolated. Following isolation of the break, the original pressurizer level will be reestablished within 75 minutes. The operator, from within the main control room, can initiate the closure of the residual heat removal isolation valves and closure will occur within 3 minutes.

5.5.4.3.2 Overpressurization Protection The residual heat removal system is equipped with two pressure relief valves, each sized to relieve the combined flow of all the charging pumps at the relief set pressure. These pressure

Revision 5209/29/2016 NAPS UFSAR 5.5-27 relief valves also serve to relieve the maximum possible back-leakage through the valves in the discharge lines separating the residual heat removal system from the reactor coolant system.

The interlocks associated with the valves on the residual heat removal inlet line from the reactor coolant system are discussed in Section 7.6.2.

5.5.4.3.3 Radiological Considerations Although the residual heat removal system is located inside the containment, the components are not adversely affected by the radiation levels normally present in the containment. The system is not required to operate in the post-accident containment atmosphere.

The operation of the residual heat removal system does not involve a radiation hazard for the operators because the system is controlled remotely from the main control room. If maintenance of a major component of the system is necessary, the portion of the system requiring maintenance can be isolated by closing manual valves. During the isolation of and maintenance on this portion of the system, the operator is exposed to a radiation dose from the reactor coolant in the system. At 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> after reaching cold shutdown conditions, the direct radiation dose received by the operator would be within 10 CFR 20 occupational limitations.

5.5.4.3.4 Cooldown Using Natural Convection The reactor coolant system is capable of being cooled via natural convection.

The following information is HISTORICAL and is not intended or expected to be updated for the life of the plant.

Diablo Canyon and Salem are prototypical of North Anna, and tests conducted at Diablo Canyon demonstrate the ability to cool down to the residual heat removal initiation by natural convection. The currently suggested time limit of 36 to 48 hours5.555556e-4 days <br />0.0133 hours <br />7.936508e-5 weeks <br />1.8264e-5 months <br /> to the residual heat removal cut-in point seems reasonable, barring unforeseen difficulties, but prototype testing at Diablo Canyon will verify the time required for this operation.

North Anna Unit 2 successfully completed the natural circulation boron mixing and cooldown test in March 1982. The test was initiated following an orderly shutdown from 100%

power for the first refueling outage. The reactor coolant was in stable condition throughout the test. Natural circulation flow developed smoothly after tripping the reactor coolant pumps.

Reactor coolant system pressure was easily controlled with pressurizer heaters and auxiliary spray. The ability to uniformly borate and cool down the reactor coolant system was demonstrated. The core exit thermocouples showed no evidence of radial tilt. The acceptance criteria of the test were met.

North Anna, since it has only one residual heat removal suction line containing two safety-grade series valves for tie-in of the reactor coolant system to the residual heat removal, might be constrained by the mechanical failure of one of these valves to open to affect the final

Revision 5209/29/2016 NAPS UFSAR 5.5-28 tie-in. In this case, the cooldown by natural convection would be continued as far as possible below the 350°F/450 psig normal tie-in point, the reactor coolant system would be depressurized as far as practical, efforts would be made to open the stuck valve (via handwheel, thermocycling, etc.), while steam dump via the steam generators is continued.

The probability of a failure of one of these valves is extremely remote. These valves are powered from different emergency power trains. The failure of either power train or of either valve operator could prevent the initiation of residual heat removal cooling in the normal manner from the control room. In the event of such a failure, operator action could be taken to open the affected valve manually. The mechanical failure of the disk separating from the stem has been investigated (Reference 3) and its probability has been found to be in the range of 10-3 to 10-4 per year. The probability of an earthquake larger than the operating-basis earthquake at North Anna is 10-2 to 10 -3 per year. The combined probability of valve stem failure coincident with the earthquake is 10-5 to 10-7 per year, so low that it need not be considered in the single-failure analysis. In the event of such a failure, the plant would remain in a safe hot standby condition with heat removal via the steam generators.

5.5.4.4 Tests and Inspections The operability of residual heat removal system active components is verified by system operation during cold shutdown and refueling shutdown conditions. The residual heat removal system is tested periodically as required by the Technical Specifications and the Technical Requirements Manual.

The instrumentation channels for the residual heat removal pump flow instrumentation devices are calibrated during each refueling operation if a check indicates that recalibration is necessary.

5.5.5 Pressurizer 5.5.5.1 Design Bases The general configuration of the pressurizer is shown in Figure 5.5-6. The design data of the pressurizer are given in Table 5.5-11. Codes and material requirements are provided in Section 5.2.

5.5.5.1.1 Pressurizer Surge Line The surge line is sized to limit the pressure drop between the reactor coolant system and the safety valves with maximum allowable discharge flow from the safety valves. (Overpressure of the reactor coolant system does not exceed 100% of the design pressure.)

The surge line is designed to withstand the thermal stresses, resulting from volume surge, that occur during operation. Administrative control of the system differential temperature is provided in plant operating curves, based on engineering analysis, for heatup and cooldown.

Revision 5209/29/2016 NAPS UFSAR 5.5-29 5.5.5.1.2 Pressurizer The volume of the pressurizer is equal to, or greater than, the minimum volume of steam, water, or total of the two that satisfies all of the following requirements:

1. The combined saturated water volume and steam expansion volume are sufficient to provide the desired pressure response to system volume changes.
2. The water volume is sufficient to prevent the heaters from being uncovered during a step-load increase of 10% at full power.
3. The steam volume is large enough to accommodate the surge resulting from the design step-load reduction of load with reactor control and steam dump without the water level reaching the high-level reactor trip point.
4. The steam volume is large enough to prevent water relief through the safety valves following a loss of load with the high water level initiating a reactor trip.
5. The pressurizer does not empty following reactor and turbine trip.
6. The emergency core cooling signal is not activated during reactor trip and turbine trip.

5.5.5.2 Design Description 5.5.5.2.1 Pressurizer Surge Line The pressurizer surge line connects the pressurizer to one reactor hot leg. The line enables continuous coolant volume pressure adjustments between the reactor coolant system and the pressurizer.

5.5.5.2.2 Pressurizer The pressurizer is a vertical, cylindrical vessel with hemispherical top and bottom heads constructed of carbon steel, with austenitic stainless steel cladding on all surfaces exposed to the reactor coolant.

The surge line nozzle and electric heaters are installed in the bottom head. The heaters are removable for maintenance or replacement. A thermal sleeve is provided to minimize stresses in the surge line nozzle. A screen at the surge line nozzle and baffles in the lower section of the pressurizer assist mixing and prevent an insurge of cold water from flowing directly to the steam/water interface.

Spray line nozzles and relief and safety valve connections are located in the top head of the vessel. Spray flow is modulated by automatically controlled air-operated valves. The spray valves also can be operated manually by a switch in the control room.

A small continuous spray flow is provided through a manual bypass valve around the power-operated spray valves to ensure that the pressurizer liquid is homogeneous with the coolant and to prevent excessive cooling of the spray piping.

Revision 5209/29/2016 NAPS UFSAR 5.5-30 During an outsurge from the pressurizer, flashing of water to steam and generating of steam by automatic actuation of the heaters keep the pressure above the minimum allowable limit.

During an insurge from the reactor coolant system, the spray system, which is fed from two cold legs, condenses steam in the vessel to prevent the pressurizer pressure from reaching the setpoint of the power-operated relief valves for normal design transients. Heaters are energized on high water level during insurge to heat the subcooled surge water that enters the pressurizer from the reactor coolant loop.

5.5.5.2.2.1 Pressurizer Support. The skirt-type support is attached to the lower head and extends for a full 360 degrees around the vessel. The lower part of the skirt terminates in a bolting flange with bolt holes for securing the vessel to its foundation. The skirt-type support is provided with ventilation holes around its upper perimeter to ensure free convection of ambient air past the heater plug connector ends for cooling.

5.5.5.2.2.2 Pressurizer Instrumentation. Refer to Chapter 7 for details of the instrumentation associated with pressurizer pressure, level, and temperature.

5.5.5.2.2.3 Spray Line Temperatures. Temperatures in the spray lines from two loops are measured and indicated. Alarms from these signals are actuated by low spray water temperature.

Alarm conditions indicate insufficient flow in the spray lines.

5.5.5.2.2.4 Safety and Relief Valve Discharge Temperatures. Temperatures in the pressurizer safety and relief valve discharge lines are measured and indicated. An increase in a discharge line temperature is an indication of leakage through the associated valve.

5.5.5.3 Design Evaluation 5.5.5.3.1 System Pressure Whenever a steam bubble is present within the pressurizer, reactor coolant system pressure is maintained by the pressurizer. Analyses indicate that proper control of pressure is maintained for the operating conditions.

A safety limit has been set to ensure that the reactor coolant system pressure does not exceed the maximum transient value allowed under the ASME Code,Section III, 1968, and thereby ensures continued integrity of the reactor coolant system boundary.

The evaluation of plant conditions of operation that follow indicate that this safety limit is not reached.

During start-up and shutdown, the rate of temperature change is controlled by the operator.

When the reactor core is shut down, the maximum heatup rate is limited by pump energy and the installed pressurizer electrical heating capacity.

Revision 5209/29/2016 NAPS UFSAR 5.5-31 When the pressurizer is filled with water (i.e., near the end of the second phase of plant cooldown and during initial system heatup), reactor coolant system pressure is maintained by the Chemical and Volume Control System.

5.5.5.3.2 Pressurizer Performance The pressurizer level is controlled to maintain a minimum free internal volume. The normal operating water volume at full-load conditions is 63% of the free internal vessel volume. Under part-load conditions, the water volume in the vessel is reduced for proportional reductions in plant load to 25% and 31% of free vessel volume at zero-power level depending on the programmed Tavg. The various plant operating transients are analyzed and the design pressure is not exceeded with the pressurizer design parameters as given in Table 5.5-11.

The reactor coolant system is normally depressurized by means of normal pressurizer spray, driven from the discharge of either reactor coolant pump A or C. However, if normal spray is not available, the system will be depressurized using the pressurizer auxiliary spray, fed through a single valve, HCV-1311 (Unit 1) or HCV-2311 (Unit 2), from the discharge of the centrifugal charging pump(s). Should this 3-inch valve fail to open following a seismic event, every effort would be made to open it via portable compressed gas cylinder or by maintenance, and if these attempts fail, system pressure could be reduced by blowing the pressurizer down through one of the two parallel power-operated relief valves provided for this purpose (PCV-1455C and PCV-1456 for Unit 1, or PCV-2455C and PCV-2456 for Unit 2). The power-operated relief valves are Seismic Class I and meet the applicable IEEE-279 standards.

5.5.5.3.3 Pressure Setpoints The reactor coolant system design and operating pressure together with the safety, power relief, and pressurizer spray valves setpoints, and the protection system setpoint pressures are listed in Table 5.5-12. The design pressure allows for operating transient pressure changes. The selected design margin considers core thermal lag, coolant transport times and pressure drops, instrumentation and control response characteristics, and system relief valve characteristics.

5.5.5.3.4 Pressurizer Spray Two separate, automatically controlled spray valves with remote manual overrides are used to initiate pressurizer spray. In parallel with each spray valve is a manual throttle valve that permits a small continuous flow through both spray lines to reduce thermal stresses and thermal shock when the spray valves open and to help maintain uniform water chemistry and temperature in the pressurizer. Temperature sensors with low alarms are provided in each spray line to alert the operator to insufficient bypass flow. The layout of the common spray line piping to the pressurizer forms a water seal that prevents steam buildup back to the control valves. The spray rate is selected to prevent the pressurizer pressure from reaching the operating setpoint of the power relief valves during a step reduction in power level of 10% of full load.

Revision 5209/29/2016 NAPS UFSAR 5.5-32 The pressurizer spray lines and valves are large enough to provide adequate spray using as the driving force the differential pressure between the surge line connection in the hot leg and the spray line connection in the cold leg. The spray line inlet connections extend into the cold-leg piping in the form of a scoop so that the velocity head of the reactor coolant loop flow adds to the spray driving force. The spray valves and spray line connections are arranged so that the spray will operate when one reactor coolant pump is not operating. The line may also be used to assist in equalizing the boron concentration between the reactor coolant loops and the pressurizer.

A flow path from the Chemical and Volume Control System to the pressurizer spray line is also provided. This additional facility provides auxiliary spray to the vapor source of the pressurizer during cooldown if the reactor coolant pumps are not operating. The thermal sleeves on the pressurizer spray connection and the spray piping are designed to withstand the thermal stresses resulting from the introduction of cold spray water.

5.5.5.3.5 Pressurizer Design Analysis The occurrences for pressurizer design cycle analysis are defined as follows:

1. The temperature in the pressurizer vessel is always, for design purposes, assumed to equal saturation temperature for the existing reactor coolant system pressure, except in the pressurizer steam space subsequent to a pressure increase. In this case, the temperature of the steam space will exceed the saturation temperature because an isentropic compression of the steam is assumed.

The only exception of the above occurs when the pressurizer is filled solid during plant start-up and cooldown.

2. The temperature shock on the spray nozzle is assumed to equal the temperature of the nozzle minus the cold-leg temperature, and the temperature shock on the surge nozzle is assumed to equal the pressurizer water space temperature minus the hot-leg temperature.
3. Pressurizer spray is assumed to be initiated instantaneously to its design value as soon as the reactor coolant system pressure increases about 40 psi above the nominal operating pressure.

Spray is assumed to be terminated as soon as the reactor coolant system pressure falls 40 psi below the normal operating pressure.

4. Unless otherwise noted, pressurizer spray is assumed to be initiated once per occurrence of each transient condition. The pressurizer surge nozzle is also assumed to be subject to one temperature transient per transient condition, unless otherwise noted.
5. At the end of each transient, except the faulted conditions, the reactor coolant system is assumed to return to a load condition consistent with the plant heatup transient.
6. Temperature changes occurring as a result of pressurizer spray are assumed to be instantaneous. Temperature changes occurring on the surge nozzle are also assumed to be instantaneous.

Revision 5209/29/2016 NAPS UFSAR 5.5-33

7. Whenever spray is initiated in the pressurizer, the pressurizer water level is assumed to be at the no-load level.

5.5.5.4 Tests and Inspections The pressurizer is designed and constructed in accordance with the ASME Code,Section III, 1968.

To implement the requirements of the ASME Code,Section XI, the following welds are designed and constructed to present a smooth transition surface between the parent metal and the weld metal. The path is ground smooth for ultrasonic inspection.

1. Support skirt to the pressurizer lower head.
2. Surge nozzle to the lower head.
3. Nozzles to the safety, relief, and spray lines.
4. Nozzle-to-safe-end attachment welds.
5. All girth and longitudinal full-penetration welds.
6. Manway attachment welds.

The liner within the safe-end nozzle region extends beyond the weld region to maintain a uniform geometry for ultrasonic inspection.

Peripheral support rings are furnished for the removable insulation modules.

The pressurizer quality assurance program is given in Table 5.5-13.

5.5.6 Pressurizer Relief Tank 5.5.6.1 Design Bases Design data for the pressurizer surge tank are given in Table 5.5-14; codes and materials of the tank are given in Section 5.2.

The tank design is based on the requirement to accept a steam discharge from the pressurizer equal to 110% of the pressurizer steam volume at full load. The tank is not designed to accept a continuous discharge from the pressurizer. The volume of water in the tank is capable of absorbing the heat from the assumed discharge, assuming an initial temperature of 120°F and increasing to a final temperature of 200°F. If the temperature in the tank rises above 120°F during plant operation, the tank is cooled by spraying in cool water and draining out the warm mixture to the boron recovery system via the primary drain transfer tank.

5.5.6.2 Design Description The pressurizer relief tank condenses and cools the discharge from the pressurizer safety and relief valves. Discharge from smaller relief valves located inside the containment is also

Revision 5209/29/2016 NAPS UFSAR 5.5-34 piped to the relief tank. The tank normally contains water and a predominantly nitrogen atmosphere; however, provision is made to permit the gas in the tank to be periodically analyzed to monitor the concentration of hydrogen and/or oxygen.

Steam is discharged through a sparger pipe under the water level. This condenses and cools the steam by mixing it with water that is near ambient temperature. The tank is equipped with an internal spray (to spray in cool primary-grade water) and a drain to the primary drain transfer tank, which are used to cool the tank following a discharge. A flanged nozzle provides a pressurizer discharge line connection.

5.5.6.2.1 Pressurizer Relief Tank Pressure The pressurizer relief tank pressure transmitter provides a signal for an indicator and provides a high-pressure alarm. A rupture disk protects the tank from excess pressure.

An analysis was performed to determine the mass that would be dumped to the pressurizer relief tank during a spurious PORV opening. The following assumptions were made, using Unit 2 setpoints:

1. The power-operated relief valves inadvertently open at 440 psig saturated in the pressurizer.
2. The power-operated relief valves close when the allowable setpoint of 370 psig is achieved.
3. Pressurizer is at 21% programmed level.

Total steam relief under these conditions was calculated to be less than 20% of the design capacity of the pressurizer relief tank. Thus, the rupture disk will remain intact.

5.5.6.2.2 Pressurizer Relief Tank Level The pressurizer relief tank level transmitter supplies a signal for an indicator and provides high- and low-level alarms.

5.5.6.2.3 Pressurizer Relief Tank Water Temperature The temperature of the water in the pressurizer relief tank is indicated, and an alarm actuated by high temperature informs the operator that cooling of the tank contents is required.

5.5.6.3 Design Evaluation The volume of water in the tank is capable of absorbing heat from the pressurizer discharge discussed in Section 5.5.6.1. Water temperature in the tank is maintained at the nominal containment temperature.

The rupture disks on the relief tank have a relief capacity equal to the combined capacity of the pressurizer safety valves. The tank design pressure is twice the calculated pressure resulting from the maximum design safety valve discharge described above. The tank and rupture disks

Revision 5209/29/2016 NAPS UFSAR 5.5-35 holders are also designed for full vacuum to prevent tank collapse if the contents cool following a discharge without nitrogen being added.

The discharge piping from the safety and relief valves to the relief tank is large enough to prevent backpressure at the safety valves from exceeding 20% of the setpoint pressure at full flow.

5.5.7 Valves Other Than Safety and Relief Valves 5.5.7.1 Design Bases As noted in Section 5.2, for all valves out to and including the second valve normally closed or capable of automatic or remote closure, valve closure time is such that for any postulated component failure outside the system boundary, the loss of reactor coolant would not prevent orderly reactor shutdown and cooldown assuming makeup is provided by normal makeup systems. Normal makeup systems are those systems normally used to maintain reactor coolant inventory under respective conditions of start-up, hot standby, operation, or cooldown. If the second of two normally open check valves is considered the boundary, means are provided to periodically assess backflow leakage of the first valve when closed. For a check valve to qualify as the system boundary, it must be located inside the containment system.

Materials of construction are specified to minimize corrosion/erosion and to ensure compatability with the environment.

Leakage is minimized to the extent practicable by design.

Valves are designed and fabricated in accordance with USAS B16.5, MSS-SP-66, and ASME Code,Section III.

5.5.7.2 Design Description All valves in the reactor coolant system that are in contact with the coolant are constructed primarily of stainless steel. Other materials in contact with the coolant, such as for hard surfacing and packing, are special materials.

All manual and motor-operated valves of the reactor coolant system that are 3 inches and larger are provided with double-packed stuffing boxes and stem intermediate lantern gland leakoff connections. All throttling control valves, regardless of size, are provided with double-packed stuffing boxes and with stem leakoff connections. All leakoff connections are piped to a closed collection system if the valve normally contains radioactive fluid and operates above 212°F. Leakage to the atmosphere is essentially zero for these valves.

Gate valves at the engineered safety features interface are either wedge design or parallel disk and are essentially straight through. The wedge may be either split or solid. All gate valves have backseat and outside screw and yoke. Globe valves T and Y style are full ported with outside screw and yoke construction. Check valves are spring-loaded lift piston types for sizes 2-1/2 inches and smaller, and swing type for sizes larger than 2-1/2 inches. All check valves that

Revision 5209/29/2016 NAPS UFSAR 5.5-36 contain radioactive fluid are stainless steel and do not have body penetrations other than the inlet, outlet, and bonnet. The check hinge is serviced through the bonnet.

The accumulator check valve is designed with a low-pressure drop configuration with all operating parts contained within the body. The disk has an imparted limited rotation to provide a change of seating surface and alignment after each valve opening.

The residual heat removal system inlet MOVs are provided with interlocks that meet the intent of IEEE-279. These interlocks are discussed in detail in Sections 5.5.4 and 7.6.2.

The isolation valves between the accumulators and the reactor coolant system boundary are provided with interlocks that meet the intent of IEEE-279 and ensure automatic valve opening when reactor coolant system pressure exceeds a specified pressure or on safety injection signal.

These interlocks are discussed in Sections 6.3.2.2.7 and 7.6.6.

The reactor coolant loop stop valves are remotely controlled motor-operated gate valves that permit any loop to be isolated from the reactor vessel. One valve is installed on each hot leg and one on each cold leg. A reactor coolant loop stop valve is shown in Figure 5.5-7. The design of the valve is basically the same as noted above with the additional feature that each set of packing can be tightened independently of the other sets of packing.

To ensure against an accidental start-up of an unborated and/or cold isolated loop, an additional valve interlock system is provided that meets the intent of IEEE-279. There is a relief line and bypass around the cold-leg isolation valve. The additional interlocks ensure that flow from the isolated loop to the remainder of the reactor coolant system takes place through the relief line valve (after system pressure is equalized through the loop drain header, and the hot-leg isolation valve is opened) for at least 90 minutes before the cold-leg stop valve is opened.

The flow through the relief line is low (approximately 200 gpm) so that the temperature and boron concentration are brought to equilibrium with the remainder of the system at a relatively slow rate. The specific loop stop valve interlocks are described in Section 15.2.6.

The parameters of each reactor coolant loop stop valve are shown in Table 5.5-15. Codes and material requirements are provided in Section 5.2.

5.5.7.3 Design Evaluation Stress analysis of the reactor coolant loop/support system, discussed in Sections 3.7 and 5.2, ensure acceptable stresses for all valves in the reactor coolant pressure boundary under every expected condition.

Reactor coolant chemistry is specified to minimize corrosion. Periodic analyses of coolant chemical composition, discussed in the Technical Requirements Manual, ensure that the reactor coolant meets those specifications.

Valve leakage is minimized by design features as discussed above.

Revision 5209/29/2016 NAPS UFSAR 5.5-37 All reactor coolant system boundary valves required to perform a safety function during the short-term recovery from transients or events considered in the respective operating condition categories will operate in less than 10 seconds.

5.5.7.4 Tests and Inspections Hydrostatic, seat leakage, and operation tests are performed on reactor coolant boundary valves as required by MSS-SP-61 and the Technical Specifications. No further test program is considered necessary.

The valve quality assurance program is indicated in Table 5.5-16.

There are no full-penetration welds within valve body walls. Valves are accessible for disassembly and internal visual inspection.

Qualification of the block valves according to requirements of NUREG-0737, Item II.D.1, is discussed in Section 5.5.8.4.

5.5.8 Safety and Relief Valves 5.5.8.1 Design Bases The combined capacity of the pressurizer safety valves is designed to accommodate the maximum surge resulting from complete loss of load. This objective is met without reactor trip or any operation action provided that the steam safety valves open as designed when steam pressure reaches the steam-side safety setting.

The pressurizer power-operated relief valves are designed to limit pressurizer pressure to a value below the fixed high-pressure reactor trip setpoint.

5.5.8.2 Design Description The pressurizer safety valves are totally enclosed pop type. The valves are spring loaded, self activated, and with backpressure compensation features.

The 6-inch pipes connecting the pressurizer nozzles to their respective code safety valves are shaped in the form of a loop seal. Condensate, a result of normal heat losses to the ambient, accumulates in the loop. The water prevents any leakage of hydrogen gas or steam through the safety valve seats. If the pressurizer pressure exceeds the set pressure of the safety valves, they start lifting, and the water from the loop seal discharges during the accumulation period.

The power relief valves are quick opening, operated automatically or by remote control.

Remotely operated stop valves are provided to isolate the power-operated relief valves if excessive leakage develops.

Two pressurizer power-operated relief valves are provided to relieve pressure from the pressurizer to the pressurizer relief tank. The valves are located downstream of isolation valves.

Revision 5209/29/2016 NAPS UFSAR 5.5-38 The power-operated relief valves protect the reactor coolant system from overpressure for a large power mismatch during the normal plant operation, and, during solid water modes at start-up, prevent actuation of the fixed high-pressure reactor trip. The operation of the power-operated relief valves also limits the undesirable opening of the spring-loaded pressurizer safety valves.

The power-operated relief valves have dual setpoints and, during normal plant operation, are controlled by containment instrument air. During solid water modes of operation, a three-way solenoid is energized and the pneumatic supply is switched to the N2 reserve tanks.

The N2 reserve tanks are subject to periodic pressure surveillance. During operating modes (MODES 1-3), sufficient pressure is maintained in the tanks to ensure that each PORV is capable of providing adequate RCS depressurization following a design basis steam generator tube rupture.

During the shutdown modes (MODES 4-6) when low-temperature overpressure protection is required, sufficient pressure is maintained in the tanks to ensure that each PORV is capable of stroking at least 120 times. This provides adequate capability to cope with an inadvertent start of a high-head safety injection pump with a water solid RCS, assuming a 10-minute response time for operator intervention to terminate the event.

Alarms are provided to protect the reactor coolant system against high pressure during start-up or shutdown and loss of reactor coolant system pressure protection which the alarms annunciate in the main control room.

The relief valve solenoids are powered from the following circuits:

Valve Solenoid 125V dc Panel/Circuit 1-RC-PCV-1455C SOV-1, 2 PNL 1A, Ckt. 23 SOV-3 PNL 1-II-A, Ckt. 1 1-RC-PCV-1456 SOV-1, 2 PNL 1B, Ckt. 23 SOV-3 PNL 1-IV-A, Ckt. 1 2-RC-PCV-2455C SOV-1, 2 PNL 2A, Ckt. 23 SOV-3 PNL 2-II-A, Ckt. 1 2-RC-PCV-2456 SOV-1, 2 PNL 2B, Ckt. 23 SOV-3 PNL 2-IV-A, Ckt. 1 During normal operation the PORV, PCV-1456 (Unit 1) and PCV-2456 (Unit 2), is closed.

Solenoid valves SOV-1456(2456)-1 and -2 admit air and SOV-1456(2456)-3 admits nitrogen to open PCV-1456(2456). The SOVs are interlocked so that air and nitrogen are not used at the same time. The operation of PCV-1455C(2455C) is similar.

Revision 5209/29/2016 NAPS UFSAR 5.5-39 The system is controlled by a keyswitch in the control room. Turning the keyswitch to the AUTO position provides low temperature overpressure protection in accordance with the Technical Specifications.

When the power-operated relief valves are being used for protection, an alarm alerting the operator of an overpressure event is provided.

Design parameters for the pressurizer spray control, safety, and power relief valves are given in Table 5.5-17.

5.5.8.3 Design Evaluation The pressurizer safety valves prevent reactor coolant system pressure from exceeding 110%

of system design pressure, in compliance with ASME Code,Section III.

A pressurizer safety valve sizing calculation was performed for North Anna Units 1 and 2 in accordance with the methodology detailed in Reference 6. In addition, an evaluation of the impact of increased pressurizer safety valve (PSV) tolerance was performed as described in Reference 11. As described there, PSV adequacy was demonstrated for accidents involving significant RCS pressurization. Of these accidents, the complete loss of external load was the most limiting. In the loss of load analysis, no credit was taken for the following:

1. Reactor trip from turbine trip.
2. Pressurizer relief valve operation.
3. Steam-line relief valve operation.
4. Steam dump system operation.
5. Reactor control system operation.
6. Pressurizer level control system operation.
7. Pressurizer spray valve operation.

In addition, the plant is assumed to be initially operating at 102% of full power and at the maximum reactor coolant system average temperature and pressure consistent with full-power operation.

The results of the calculation show a peak pressure less than the design criterion of 2750 psia.

For the overpressure analysis, an average setpoint tolerance for the reactor coolant system safety valves of +2% and maximum tolerance for any valve of +3% was used. No credit is taken for automatic actuation of the reactor coolant system power-operated relief valves in any accident analyses; as a result, a setpoint tolerance is not specified. In addition, the power-operated relief valves are used manually by the operator at various pressures.

Revision 5209/29/2016 NAPS UFSAR 5.5-40 The pressurizer power relief valves prevent actuation of the fixed reactor high-pressure trip for all design transients up to and including the design step-load decrease (50% of full load) with steam dump. The relief valves also limit undesirable opening of the spring-loaded safety valves.

Flow-induced transient dynamic loads caused by rapid opening of the pressurizer safety and relief valves are considered in the design of the pressurizer relief piping system. These forcing functions are based on Westinghouse System Standard No. 1.3, Systems Standard Design Criteria Nuclear Steam Supply System Design Transients (October 1972), which includes the effect of water slugs arising from the loop seals. The limiting number of actuations for the power-operated relief valves is 70 based on the fatigue evaluation. This limitation supersedes 320 PORV actuations described in Westinghouse System Standard 1.3.

A time-history dynamic analysis was performed by using the above calculated forcing functions to compute the responses (deflections, reactions, and stresses) of this piping system.

These loadings are classified as occasional mechanical loads in Subarticle NB-3600 of the ASME Code,Section III, which are included in the piping analysis under applicable design conditions.

The pressurizer safety valve restraint was designed to withstand seismic, thermal, and deadweight forces, in addition to fluid transient loads that occur during operation of the pressurizer safety valve. The restraint is designed for all possible force and moment combinations tending to produce axial, plane bending, torsional, and shear stresses. The restraint itself consists of the following:

1. Two circumferential anchor straps around the pressurizer vessel.
2. Two built-up box sections that are welded to each other and are bolted to the anchor strap.
3. A flange welded to the box section and bolted to the safety valve flange.

Each of the pressurizer power relief valves located farthest outboard of the pressurizer vessel is restrained in the vertical direction using a welded framework. This restraint and the relief valve discharge piping system is designed to accommodate all sustained/transient primary and secondary loading conditions, including thermal expansion, deadweight, seismic, and relief valve discharging loads.

5.5.8.4 Tests and Inspections The testing performed on safety and relief valves, other than operational tests and inspections, is the required hydrostatic, seat leakage, and operation tests. Also, the safety backup nitrogen supply for the power-operated relief valves is tested to ensure that the power-operated relief valves can function on the loss of normal air and nitrogen supplies. These tests ensure that the valves will operate as designed.

There are no full-penetration welds within the valve body walls. Valves are accessible for disassembly and internal visual inspection.

Revision 5209/29/2016 NAPS UFSAR 5.5-41 In accordance with the requirements of NUREG 0737, Item II.D.1, concerning performance testing and evaluation of relief, safety and block valves and associated discharge piping analysis, VEPCO has responded to the performance testing and plant-specific evaluations in References 4 and 5. Piping analysis has been completed and necessary modifications have been implemented.

5.5.9 Reactor Coolant System Equipment Supports 5.5.9.1 Design Basis The reactor coolant system includes the reactor vessel, three steam generators, three reactor coolant pumps, and a pressurizer. Structures are provided to support this equipment to ensure system integrity during normal operation, design basis accident conditions, and seismic events.

All supports in the reactor coolant system are designed to withstand the effects of horizontal and vertical design-basis earthquake acting simultaneously with an instantaneously applied pipe rupture in addition to normal operating loads. Loads due to pressure, deadweight and thermal are combined algebraically and then added directly to the Square Root of the Sum of Squares (SRSS) of SSE and the worst effect postulated main steam line break, main feedwater line break, or reactor coolant loop branch line (RHR, Pressurizer Surge, accumulator) break to determine combined loads. The values of dynamic hydraulic loads for any reactor coolant branch line rupture are based on the Westinghouse blowdown analysis. A single-loop analysis has been performed to ensure that no stresses in the supports exceeded 90% of the yield point of the structural material used. A Significant margin of safety is established on each supporting component.

The combination of design-basis earthquake, pipe rupture, and deadweight loads is comparable to the combination of loads considered to be a faulted condition under the present ASME Code,Section III. No such definition of load categories existed at the time the supports were designed and no applicable ASME Code for component supports was in effect as of January 1973. This extreme combination of loads based on a detailed dynamic analysis was used as the basis for the stress analysis. The normal operating loads were calculated and, since the magnitude of these loads was small when compared with the accident loads, a stress analysis for the normal operating condition was not performed.

All welding is in accordance with Section IX of the ASME Code, AWS as appropriate, and all welds are examined by radiographic, ultrasonic, dye penetrant, or magnetic particle techniques.

The primary equipment supports for the faulted condition are designed to a maximum stress limit of 90% of the yield point of the structural material used. Comparing this stress allowable criterion with that of Subsection NF of ASME Code,Section III, shows that the basic support materials used (A-36 and A-537-type material) provide a more conservative design and that stresses in the high-strength bolting and clevis materials (A-574 and A-340-type material) are less conservative than the material yield criteria of ASME Code,Section III.

Revision 5209/29/2016 NAPS UFSAR 5.5-42 Normal and upset condition loads can be determined by the deletion of the pipe rupture loads from the design loads used. Operating-basis earthquake and design-basis earthquake have been concluded to yield generally similar loads that are a small percentage of the total design load. On the basis of this load comparison, the satisfaction of Subsection NF for normal and upset operating loads has been concluded. Compliance with the various design rules specified in Subsection NF is satisfactory. There are some materials and dimensional details used that are not currently listed; however, they are conservative.

5.5.9.2 Description 5.5.9.2.1 Reactor Vessel Support The reactor vessel is supported by six sliding foot assemblies mounted on the neutron shield tank as shown in Figure 5.5-8. These foot assemblies were fabricated from modified AISI 4330 steel forgings. The support feet are designed to restrain seismic movement of the reactor vessel, while allowing radial thermal expansion. The neutron shield tank is a double-walled cylindrical structure of ASTM A516, Grade 60 steel that transfers the loadings to the heavily reinforced concrete mat and internal structures of the containment building. The tank also serves to minimize gamma and neutron heating of the primary concrete shield, and to attenuate neutron radiation outside of the primary shield to acceptable limits.

The shield tank is securely fastened by anchor bolts. Overturning moments and horizontal forces induced on the tank during normal operation or accident condition are taken by the shield tank anchor bolts and the reinforced-concrete primary shield wall poured around the neutron shield tank. Any resulting vertical force and torque is taken by the anchor bolts.

The tank was completely shop fabricated and was constructed in accordance with applicable portions of Section VIII, Division 2 (1968) of the ASME Code. However, a code stamp is not required because it is not within the code jurisdiction. All welding procedures and welding operator qualifications were in accordance with Section IX of the ASME Code.

After fabrication, the completed tank was subjected in the vertical position to a hydrostatic test of 25 psig as measured on top of the tank. In no case did the hydrostatic pressure exceed 35 psig anywhere in the tank. The tank was also leak tested with dry air at 20 psig by applying soapsuds to all welds accessible from the outside of the tank.

5.5.9.2.2 Steam Generator and Reactor Coolant Pump Supports The steam generator and reactor coolant pump supports are shown in Figures 5.5-9 and 5.5-10, and the load paths into the reinforced concrete are shown in Figure 5.5-11. The materials used were for the most part commercially available structural shapes of A36 steel.

High-strength quenched and tempered alloy steels were used for local attachments at the steam generator support pads, in the hydraulic snubbing assemblies, and in the pump support columns.

Revision 5209/29/2016 NAPS UFSAR 5.5-43 The steam generator support system consists of an upper support ring and a lower support frame. The upper support ring was shimmed in the cold condition to the steam generator with a sufficient radial gap to permit full-pressure expansion of the steam generator and insulated so that it expands thermally as the steam generator is brought up to temperature. The upper support ring transmits horizontal forces from the steam generator through four tangential load trains to the reinforced-concrete charging floor. The charging floor in turn transmits these horizontal forces to the reactor shield wall, the crane wall, and the cubicle walls, where, through shearing actions, it is further transmitted downward to the mat. A 4-ft. 8-in. octagonal concrete column between the cubicle floor and the mat beneath the steam generator provides an additional load path that transmits some of the vertical forces directly from the cubicle floor to the mat. The two tangential load trains from the upper support ring to the charging floor parallel to the hot leg of the reactor coolant loop are equipped with hydraulic snubbing cylinders that permit limited slow motion of the steam generator to allow for thermal expansion of the reactor coolant piping from the reactor to the steam generator. However, the cylinders react to resist suddenly applied forces that occur from earthquake and/or pipe rupture conditions. The other two tangential loads trains from the upper support ring to the charging floor act in a direction perpendicular to the direction of the reactor coolant loop hot leg. Since the movement in that direction is not significant, two strut members are designed to resist applied forces primarily from earthquake and/or postulated pipe rupture conditions.

The lower support frame is a weldment fabricated of A36 and A572 structural steel shapes.

The support frame slides on lubricated bearing plates located under each corner column to permit thermal expansion of the reactor coolant piping from the reactor to the steam generator. The four columns also transmit vertical forces from the steam generator to the cubicle floor. The support frame has large shear blocks on two slides that fit into embedments in the cubicle floor. These shear blocks guide the lower support frame along a direction radial from the reactor and transmit forces perpendicular to this motion into the embedments in the cubicle floor. The attachment of the lower support frame to the four pads on the steam generator bottom head permits radial thermal expansion of the steam generator.

The inservice inspection of external supports for reactor coolant system vessels is in accordance with ASME Section XI. Additionally, to periodically verify the integrity of the lower steam generator supports, all accessible main member-to-member welds joining A572 material will be visually examined during each inservice inspection interval, as controlled by the Augmented Inspection Manual. Main member welds are those joining the wide flange members to each other, and do not include welds on gussets, cover plates, etc. The same time schedule as required for vessel nozzles will be used.

The reactor coolant pump is mounted in a support frame that permits radial thermal expansion of the pump feet. The frame is held above the cubicle floor by three pin-ended columns that provide vertical support while allowing free movement in the horizontal plane. Lateral support for the pump is provided by two hydraulic snubbing assemblies between the pump

Revision 5209/29/2016 NAPS UFSAR 5.5-44 support frame and the steam generator lower support frame. These snubbing assemblies permit slow horizontal movement of the pumps for thermal expansion of reactor coolant piping between the pump and the steam generator but react to suddenly applied forces from an earthquake and pipe rupture.

The vertical forces applied to the cubicle floor are carried by the reinforced concrete to the edges of the floor where the vertical forces are transmitted to the surrounding walls. The vertical forces transmitted to the cubicle walls are in turn transmitted out to the crane wall columns and to the shield walls where they are carried downward to the mat.

Horizontal forces applied to the cubicle floor act as torsional moments about the centerline of the reactor. This moment is transmitted to the mat by torsional shearing forces in the shield wall and by shear forces in the crane wall columns and in the column below the steam generator.

5.5.9.2.3 Pressurizer Support The pressurizer vessel is mounted to a rigid ring girder that is suspended from the charging floor by four hanger columns as shown in Figure 5.5-12. Two brackets welded to the ring girder slide in guides rigidly attached to the wall, which restrain all motions except vertical translation.

In addition, antisway brackets welded to the shell of the pressurizer fit into striker plate assemblies embedded in the concrete floor close to the center of gravity of the vessel. These brackets permit the pressure vessel to expand vertically but restrain horizontal displacements.

The ring girder is fabricated from ASTM A516, Grade 70 steel and the striker plate assemblies are fabricated from ASTM A543, Grade B, Class II steel. The hanger columns are fabricated from ASTM A106, Grade B pipe. The majority of the fasteners and shear pins used in the support are fabricated from either ASTM A193, Grade B7, or ASTM A540, Grade B23, depending on the stress level.

5.5.9.3 Evaluation 5.5.9.3.1 Steam Generator and Reactor Coolant Pump Supports Dynamic analyses were performed to determine loads on the support structures and components resulting from rupture of the branch lines to the reactor coolant piping (RHR, Pressurizer Surge, Accumulator lines), main steam lines and main feedwater lines and design-basis horizontal and vertical earthquakes. The combined loadings were obtained by first algebraically summing the loads due to pressure, deadweight, and thermal and then by directly adding that to SRSS of SSE and the worst effect of postulated main steam line break, main feedwater line break or reactor coolant loop branch line (RHR, Pressurizer Surge, Accumulator) break.

The dynamic model for a loop as indicated in Figure 5.5-13 includes the steam generator, reactor coolant pump, associated piping, and supports as a coupled system. To complete the model, the inlet and outlet nozzles of the reactor vessel were assumed to be rigidly attached to the

Revision 5209/29/2016 NAPS UFSAR 5.5-45 vessel. The mass and stiffness characteristics of each of the major subsystems were accurately transformed to a lumped parameter system. Approximately 80 nodes (450 static degrees of freedom) were employed in the dynamic model representation.

Natural frequencies, characteristic mode shapes, and modal participation factors were calculated for the undamped multidegree of freedom combined structural system using the NUPIPE-SW computer program. The dynamic loading conditions were specified as spatial load vectors and associated time histories. The step-by-step direct integration method was employed to obtain a time history of forces and displacements for the pipe rupture solution. The Normal Mode Method, combined with the square root of the sum of the squares approach, was used to determine the seismic response of the system.

The forcing functions used in the dynamic pipe rupture analysis were supplied by Westinghouse. The data consisted of time-history hydraulic forcing functions given at several points in the reactor coolant loop where changes in flow direction for flow area occur. Amplified response spectra were employed to determine the seismic responses.

Since the dynamic model indicated in Figure 5.5-13 is an idealization of the support structure and equipment shown in Figure 5.5-9, the results of the dynamic analysis could not be used directly. Instead, the time history of displacements obtained from the dynamic analysis were applied to a more detailed static analysis model to obtain internal loads and stresses in the support structure, loads on the equipment support pads, and loads on the reinforced-concrete structure that interface with the equipment supports. This stress model is shown in Figure 5.5-14.

Since Westinghouse is responsible for the design of the reactor coolant loop system, a final verification dynamic analysis was performed by Westinghouse subsequent to the completion of the steam generator and reactor coolant pump support design.

These analyses were completed and the results indicated that no stresses exceeded 90% of the yield point of the structural material used. Tables 5.5-18, 5.5-19, and 5.5-20 contain dynamic loads for some of the components. Nondynamic effect such as thermal gradients produced in the supports by pipe rupture jet impingement were also investigated. A horizontal longitudinal split in the reactor coolant hot leg, for example, produces an average temperature in the flange of the nearest support member of approximately 250°F. This and other locations of the supports have been examined for the effects of thermal gradients.

5.5.9.3.2 Reactor Vessel Supports, Neutron Shield Tank, and Pressurizer Supports For the determination of dynamic loads on the reactor vessel supports, the neutron shield tank, and the pressurizer supports, an analysis technique was applied that is similar to that used for the steam generator and reactor coolant pump supports. However, for the reactor vessel supports and neutron shield tank, the STRUDL program (developed by the MIT Civil Engineering Department) was used.

Revision 5209/29/2016 NAPS UFSAR 5.5-46 The dynamic models used in the analysis of the pressurizer supports and reactor vessel supports are shown in Figures 5.5-15 and 5.5-16, respectively.

5.5.9.3.3 Snubber Design and Qualification of Hydraulic Cylinders for North Anna Power Station Units 1 and 2.

General Description The reactor coolant system snubbers are hydraulic units including a hydraulic cylinder with piston, piston rod, flow control devices, cylinder end lug (paddle) with bearings to fit into the wall bracket (clevis), and a self-contained fluid reservoir. The hydraulic cylinder has a threaded rod end to interface with extension pieces to make the unit the appropriate length for the application.

Two sizes of snubbers are used. The snubbers installed between the lower steam generator support and reactor pump support frame are designed with a normal capacity of 448 kips and a faulted load capacity of 1000 kips, while those installed to restrain the upper steam generator are designed with a normal load capacity of 1124 kips and a faulted load capacity of 1900 kips.

The specified environmental limits of the hydraulic snubbing cylinders for continuous duty are as follows:

Temperature Range: 70 - 120°F Max Radiation Exposure: 3.0 x 107 Rads Relative Humidity: 30 - 100%

Ambient Pressure: 8.9 - 11.8 psia Snubber Description and Operation The reactor coolant system primary equipment snubbers are hydraulic units using the movement of a piston and internal valves to control the speed with which the snubber extends or contracts. During normal operation, the piston is free to move in both directions after overcoming a static load equal to or less than 15 kips for the 1000-kip units and 19 kips for the 1900-kip units.

The total stroke is greater than or equal to 5 inches to provide adequate motion in both the tension and compression direction of the piston rod.

When a dynamic event such as a seismic event or pipe rupture occurs, there is a pressure buildup due to the velocity of the supported component. This exerts enough force on the control valves to overcome the biasing spring force holding the valve open. This causes the valves to close and the snubber to lock up, restraining the equipment to which it is attached.

Bleed rates are achieved when the snubber locks up and a unidirectional force remains.

All materials used in the snubbers are selected with particular attention being given to the application for which they are intended and the environmental conditions which they will see. All components are corrosion resistant. Metallic components are stainless steel and brass alloy. Seals

Revision 5209/29/2016 NAPS UFSAR 5.5-47 are selected for their long life and resistance to the radiation and temperature conditions to be experienced. Silicone-based hydraulic fluid is used to withstand the radiation, temperature, and pressure conditions for which the snubbers are designed.

Development Tests The hydraulic snubbers have been subjected to a rigorous series of qualification tests. The results of the test series proved that the 1000-kip snubber can withstand 1.1 x 106 lb and the 1900-kip snubber can withstand 2.09 x 106 lb. Sample units were disassembled after the tests and component parts examined. The results of the examination indicated that the parts were in good working order.

All units were subjected to acceptance tests to verify load capacity, lockup rate, bleed rates and the running drag in both tension and compression direction.

5.5.10 Reactor Coolant Vent System The reactor coolant high-point vent system conforms to the requirements set forth in Section II.B.1 of NUREG-0737 entitled, Clarification of TMI Action Plan Requirements.

The basic function of the reactor coolant vent system is to remove non-condensables or steam from the reactor vessel head and the pressurizer. The system is designed to mitigate inadequate core cooling, inadequate natural circulation flow, and inability to depressurize to the RHRS initiation conditions resulting from the accumulation of noncondensable gases in the reactor coolant system.

5.5.10.1 Design Bases The reactor coolant vent system design bases are as follows:

  • Vent the reactor vessel and pressurizer with any limiting single active failure.
  • Isolate a system venting operation with any limiting single active failure.
  • Allow a reasonable venting time without developing unacceptable levels of bulk combustible gas concentrations in the containment.

5.5.10.2 Design Description The reactor coolant vent system provides the capability to vent the reactor vessel or the pressurizer using only safety-related equipment. The active portion of the vent system consists of four 1-inch open/close solenoid-operated isolated valves. The isolation valves are powered by vital dc power supplies and are fail-closed active valves in compliance with the NRC Regulatory Guide 1.48.

Revision 5209/29/2016 NAPS UFSAR 5.5-48 The reactor vessel vent system connects to a part-length control rod drive housing above the seismic support platform. The vent system piping connects to the control rod housing via a special plug adapter connection, machined to reduce the vent piping to 1-inch, schedule 160 (0.815 inch i.d.). The reactor vessel head vent piping then divides into two flow paths each supported by the seismic support platform. Each flow path contains a 3/8-inch orifice and two remotely-operated isolation valves in series. The two flow paths are reconnected downstream of the second isolation valve in each flow path. The common downstream piping then continues around the seismic support platform where a short section of piping would direct vented fluid toward the fuel transfer canal/refueling cavity area.

The common vent pipe upstream from the remotely operated valves contains a manual globe valve. This valve is administratively controlled open during normal power operation, but may be closed for refueling or maintenance.

The pressurizer vent system connects to the pressurizer vapor sample line. Like the reactor vessel head vent system, it utilizes a normally open, manual, existing globe valve. Parallel flow paths containing remotely-operated solenoid valves were added. Vent system connection to the existing sample piping is accomplished by the installation of a tee downstream of the manual globe valve. A 3/4-inch by 1-inch reducer connects this piping to the common 1-inch vent piping upstream of the solenoid-operated globe valves. A water seal is provided on the inlet side of the isolation valves to minimize the possibility of seat leakage. As in the reactor vessel vent system, the parallel pressurizer flow paths are reconnected downstream of the second isolation valve in each flow path. This common vent piping runs along the inside crane wall and discharges into the fuel transfer canal.

The isolation valves in series in each parallel flow path are powered by the same vital 125V dc power supply. Similarly, series valves in the alternate parallel path are powered by the vital dc bus energized from the redundant power train. The power supplies for these valves are backed-up by the battery. All valves will fail closed on loss of power. Operation of the reactor coolant vent system will be conducted from the control room of each unit. Valve control switches and positive valve position indicator lights (open-shut) are located on the post-accident monitor and control panel.

The piping and vent material in contact with reactor coolant water is austenitic stainless steel, compatible with the reactor coolant chemistry shown in Table 5.2-25.

The reactor vessel head vent piping and fittings up to and including the 3/8-inch orifices constitute an extension of the reactor coolant pressure boundary, and are designed and fabricated to meet the code requirements of ANSI-B31.7 as Class 1 nuclear piping and fittings (VEPCO-Q1). That portion of the reactor vessel head vent from the 3/8-inch orifices up to and including the second isolation valve in each parallel flow path is designed and fabricated to meet the code requirements of ANSI B31.7 as Class 2 nuclear piping (VEPCO Q2).

Revision 5209/29/2016 NAPS UFSAR 5.5-49 The solenoid-operated isolation valves in both the reactor vessel head and pressurizer vent lines are designed and qualified to meet the following requirements:

1. NRC Regulatory Guide 1.48 - Design Limits and Loading Combinations for Seismic Class I Fluid System Components.
2. Design pressure - 2485 psig.
3. Design temperature - 650°F.
4. ASME Section III, 1977 Safety Class 2
5. IEEE-323-1974Equipment Qualification IEEE-344-1975Seismic Testing IEEE-382-1972Guide for Type Test of Class 1 Electrical Valve Operators for Nuclear Power Generating Stations.

All solenoid-operated isolation valves are designed to meet environmental qualifications under normal, transient, and accident conditions.

The pressurizer vent piping connects to the existing line 3/4-RC-51-Q1. Failure of this piping does not constitute a loss-of-coolant accident as venting steam through a 3/4-inch line is equivalent to venting water through a 3/8-inch orifice and the reactor can be shut down and cooled down in an orderly manner assuming water makeup is provided by the normal charging system. A safety class transition from Q1 to Q2 is made at the 3/8-inch orifice in this line. All piping and fittings from the orifice to the second isolation valve in each flow path is designed and fabricated to meet the code requirements of ANSI-B31.7 as Class 2 nuclear piping (VEPCO Q2).

Portions of the reactor vessel head and pressurizer vent systems downstream of the second isolation valve up to vent piping termination to the fuel transfer canal/refueling cavity area meet the requirements of ANSI-B31.1 (VEPCO Non-Q). The entire reactor coolant vent system is seismically supported.

There are no removable sections in the reactor vessel head vent system, and, except for cable disconnection, the system remains intact during head removal.

The reactor coolant vent system will be manually operated only during accident conditions which require venting of steam or noncondensable gases to ensure adequate core cooling.

Explicit administrative controls and operating procedures dictate when the vent system will be operated as well as conditions under which the system will not be operated. Operating guidelines were submitted to the NRC by Reference 10.

5.5.10.3 Design Evaluation The combination of valve failure modes and power supply assignments allows the reactor head vent system and the pressurizer vent system to meet the single-active-failure criteria for

Revision 5209/29/2016 NAPS UFSAR 5.5-50 venting initiation and isolation. By procedure, the venting operation will use only one of the four available flowpaths provided by the reactor coolant system (two parallel paths on the vessel head and two parallel paths on the pressurizer) at any one time. Redundant power supplies are provided so that the failure of a power supply powering one vent path will not affect the operation of the valves in the parallel flow path. Likewise, a valve mechanically failing in one flowpath is addressed by opening the parallel path. If a single valve mechanically fails in the open position, the valve in series may be used to terminate the vent flow. The design provides that, for the very unlikely event of both series valves in a vent path failing open, the in-line orifice will restrict the vent rate and loss of coolant such that one charging pump can adequately provide makeup.

The system design with two valves in series in each flow path minimizes the possibility of reactor coolant pressure boundary leakage. Leakage can be detected by an increase in the amount of makeup required to maintain a normal level in the pressurizer. Leakage inside the containment is drained to the containment sump where it is monitored. Leakage is also detected by measuring the airborne activity of the containment atmosphere and monitoring the containment pressure.

The valves are normally closed, deenergized, and therefore maintain their deenergized position following a loss of power. Because there are two normally closed, deenergized valves in series in each flow path, power lockout to the valves at the control board is not considered.

Each flow path in the reactor vessel head vent is orificed to 3/8 inch to provide a safety class transition from Q1 to Q2. A postulated break, downstream from the orifice, or an inadvertently open flow path, is flow limited to the capacity from one centrifugal charging pump. The break of the reactor coolant vent system piping upstream from the orifice is defined as a loss-of-coolant accident. The 3/8-inch orifice also limits the flow of hydrogen from the reactor coolant system to allow a reasonable venting period without exceeding bulk containment combustible limits.

The following considerations were addressed in evaluating a suitable location for vent piping termination within the containment:

1. Conditions under which venting will be initiated.
2. Expected composition of vented fluid.
3. Fluid impingement on piping and components.

The primary function of the reactor coolant vent system has been defined as providing the operator an additional means of ensuring adequate core cooling when the presence of large amounts of steam and/or noncondensables may inhibit such cooling.

Since the generation of large amounts of hydrogen in the core could be associated with a breach of fuel cladding integrity, a significant release of fission products to the primary coolant and thus to the containment may be expected. However, vent system operation will not contribute to a condition where containment integrity would be compromised.

Revision 5209/29/2016 NAPS UFSAR 5.5-51 As discussed earlier, venting initiation and termination will be dictated by the stable bulk hydrogen concentration in containment, which will be controlled so as not to exceed 4% as a result of vent system operation.

Both reactor coolant vents will discharge into the fuel transfer canal/refueling cavity area.

High pressure fluid discharged to this general area will not pose an impingement hazard. A loop seal is maintained in the pressurizer vent line. The operation of the pressurizer vent path will result in a water slug traveling down the piping, which will result in sizable pipe stress loads. Pipe support designs assume conservatively high-water slug loads for the design of supports.

5.5.10.4 Tests and Inspections Procedures will be developed to periodically test the operability of the reactor coolant vent system.

The operability testing of the reactor coolant vent system valves will be performed in accordance with the ASME Code for Category B valves.

Revision 5209/29/2016 NAPS UFSAR 5.5-52

5.5 REFERENCES

1. Letter, VEPCO to NRC,

Subject:

Evaluation of Thermal Sleeve Failure, Unit 1, dated October 12, 1982 (Serial No. 574).

2. Letter, VEPCO to NRC,

Subject:

Evaluation of RCS Piping Thermal Sleeves, Unit 2, dated August 4, 1982 (Serial No. 460).

3. R. A. Hill, J. F. OBrien, D. C. McIntire, and R. T. Barlow, Evaluation of Mispositioned ECCS Valves, WCAP 9207, 1972.
4. Letter from R. H. Leasburg, VEPCO, to H. R. Denton, NRC,

Subject:

Relief Safety, Block Valve Test and Discharge Piping Analysis Requirements, dated July 1, 1982 (Serial No. 392).

5. Letter from R. H. Leasburg, VEPCO, to H. R. Denton, NRC,

Subject:

Relief, Safety, Block Valve Test and Discharge Piping Analysis Requirements, dated September 1, 1982 (Serial No. 514).

6. K. Cooper, et al., Overpressure Protection for Westinghouse Pressurized Water Reactors, WCAP-7769, Revision 1, 1972.
7. R. Salvatori, Pipe Break for the LOCA Analysis of the Westinghouse Primary Coolant Loop, WCAP 8082, June 1973 (proprietary).
8. R. Salvatori, Pipe Break for the LOCA Analysis of the Westinghouse Primary Coolant Loop, WCAP 8172, January 1975 (nonproprietary).
9. Letter VEPCO to NRC, dated August 26, 1976 (Serial No. 212).
10. Letter from R. H. Leasburg, VEPCO, to H. R. Denton, NRC,

Subject:

Request for Additional Information, Reactor Coolant System Vents, dated April 23, 1982 (Serial No. 127).

11. Letter from James P. OHanlon, Virginia Power, to NRC, Proposed Technical Specification Change, Increased Pressurizer Safety Valve Lift Setpoint Tolerance, dated July 26, 1995 (Serial No.95-366).
12. Nuclear Safety Advisory Letter NSAL 99-005, Reactor Coolant Pump Operation During a Loss of Seal Injection, 6/1/99.

Revision 5209/29/2016 NAPS UFSAR 5.5-53 5.5 REFERENCE DRAWINGS The list of Station Drawings below is provided for information only. The referenced drawings are not part of the UFSAR. This is not intended to be a complete listing of all Station Drawings referenced from this section of the UFSAR. The contents of Station Drawings are controlled by station procedure.

Drawing Number Description

1. 11715-FM-093A Flow/Valve Operating Numbers Diagram: Reactor Coolant System; Loops 1, 2, & 3; Unit 1 12050-FM-093A Flow/Valve Operating Numbers Diagram: Reactor Coolant System; Loops 1, 2, & 3; Unit 2
2. 11715-FM-093B Flow/Valve Operating Numbers Diagram: Reactor Coolant System, Unit 1 12050-FM-093B Flow/Valve Operating Numbers Diagram: Reactor Coolant System, Unit 2
3. 11715-FM-093E Flow/Valve Operating Numbers Diagram: Reactor Coolant Pump Oil Collection, Unit 1 12050-FM-093E Flow/Valve Operating Numbers Diagram: Reactor Coolant Pump Oil Collection, Unit 2
4. 11715-FM-094A Flow/Valve Operating Numbers Diagram: Residual Heat Removal System, Unit 1 12050-FM-094A Flow/Valve Operating Numbers Diagram: Residual Heat Removal System, Unit 2

Revision 5209/29/2016 NAPS UFSAR 5.5-54 Table 5.5-1 REACTOR COOLANT PUMP DESIGN PARAMETERS Parameter Value Design pressure 2485 psig Design temperature 650°F Capacity/pump 92,800 gpm Developed head 312 ft NPSH required 170 ft Suction temperature 546.5°F RPM nameplate rating 1200 Discharge nozzle, i.d. 27-1/2 in.

Suction nozzle, i.d. 31 in.

Overall unit height 25 ft. 6 in.

Water volume 56 ft3 Moment of inertia 95,000 ft2-lb Weight, dry 179,500 lb Motor Type ac, induction, single-speed, air-cooled Power 7000 hp Voltage 4000 Insulation class B thermolastic epoxy Phase 3 Frequency 60 Running (nominal values)

Current, hot amp 860 Current, cold amp 1123 Input (hot reactor coolant) 5493 kW Input (cold reactor coolant) 7087 kW Motor air-to-water coolers 2 Seal water injection 8 gpm Seal water return 1-RC-P-1A & -1B; 2-RC-P-1A, 1B, & 2.5 gpm 1C Seal water return 1-RC-P-1C 3 gpm

Revision 5209/29/2016 NAPS UFSAR 5.5-55 Table 5.5-2 REACTOR COOLANT PUMP QUALITY ASSURANCE PROGRAM Examination RT UT PT MT Castings Yes Yes Forgings Main shaft Yes Yes Main studs Yes Yes Flywheel (rolled plate) Yes Yes (for base)

Weldments Circumferential Yes Yes Instrument connections Yes Key: RT = radiographic UT = ultrasonic PT = dye penetrant MT = magnetic particle Table 5.5-3 STEAM GENERATOR DESIGN DATA Parameter Value Design pressure, reactor coolant side 2485 psig Design pressure, steam side 1085 psig Design temperature, reactor coolant side 650°F Design temperature, steam side 600°F Total heat transfer surface area 54,500 ft2 Maximum moisture carryover 0.10 wt%

Overall height 67 ft. 8 in.

Number of U-tubes 3592 U-tube o.d. 0.875 in.

Tube wall thickness, nominal 0.050 Number of manways 4 I.d. of manways 16 in.

Number of handholes 6 I.d. of handholes 6 in.

Number of inspection ports 2 I.d. of inspection port 4 in.

Revision 5209/29/2016 NAPS UFSAR 5.5-56 Table 5.5-4 STEAM GENERATOR QUALITY ASSURANCE PROGRAM Examination RT UT PT MT ET Tubesheet Forging Yes Yes Cladding Yesa Yesb Channel head Casting Yes Yes Forging Yes Yes Cladding Yes Yes Secondary shell and head Plates Yes Forgings Yes Tubes Yes Yes Nozzles (forgings) Yes Yes Weldments Shell, longitudinal Yes Yes Shell, circumferential Yes Yes Cladding (channel head-tubesheet Yes Yes joint cladding restoration)

Steam and feedwater nozzle to shell Yes Yes Support brackets Yes Tube to tubesheet Yes Instrument connections (primary and Yes secondary)

Temporary attachments after removal Yes After hydrostatic test (all welds Yes where accessible)

Nozzle safe ends (if forgings) Yes Yes Nozzle safe ends (if weld deposit) Yes Key: RT = radiographic UT = ultrasonic PT = dye penetrant MT = magnetic particle ET = eddy current

a. Flat surfaces only.
b. Weld deposit areas only.

Revision 5209/29/2016 NAPS UFSAR 5.5-57 Table 5.5-5 REACTOR COOLANT PIPING DESIGN PARAMETERS Parameter Value Reactor inlet piping, i.d. 27-1/2 in.

Reactor inlet piping, nominal wall thickness 2.32 in.

Reactor outlet piping, i.d. 29 in.

Reactor outlet piping, nominal wall thickness 2.44 in.

Coolant pump suction piping, i.d. 31 in.

Coolant pump suction piping, nominal wall thickness 2.59 in.

Pressurizer surge line piping, i.d. 11.18 in.

Pressurizer surge line piping, nominal wall thickness 1.406 in.

Water volume, all loops and surge line 1455 ft3 Design/operating pressure 2485/2235 psig Design temperature 650°F Design temperature (pressurizer surge line) 680°F Design pressure and temperature of pressurizer relief line From pressurizer to safety valve 2485 psig, 650°F From safety valve to pressurizer relief tank 600 psig, 650°F Table 5.5-6 REACTOR COOLANT THERMAL SLEEVE REMOVAL Unit 1 Line Numbera To Line Numbera 6 in.-RC-17-1502-Q1 27-1/2 in.-RC-3-2501R-Q1 (loop 1) 3 in.-CH-1-1502-Q1 27-1/2 in.-RC-6-2501R-Q1 (loop 2) 12 in.-RC-23-1502-Q1 27-1/2 in.-RC-6-2501R-Q1 (loop 2)

Unit 2 Line Numbera To Line Numbera 12 in.-RC-423-1502-Q1 27-1/2 in.-RC-406-2501R-Q1 (loop 2) 12 in.-RC-424-1502-Q1 27-1/2 in.-RC-409-2501R-Q1 (loop 3) 3 in.-CH-401-1502-Q1 27-1/2 in.-RC-406-2501R-Q1 (loop 2) 6 in.-RC-420-1502-Q1 27-1/2 in.-RC-409-2501R-Q1 (loop 3)

a. Lines are identified in Reference Drawings 1 through 3.

Revision 5209/29/2016 NAPS UFSAR 5.5-58 Table 5.5-7 REACTOR COOLANT PIPING QUALITY ASSURANCE PROGRAM Examination RT UT PT Fittings and pipe (castings) Yes Yes Fittings and pipe (forgings) Yes Yes Weldments Circumferential Yes Yes Nozzle to runpipe (except no RT for nozzles less than 4 in.) Yes Yes Instrument connections Yes Key: RT = radiographic UT = ultrasonic PT = dye penetrant Table 5.5-8 DESIGN BASES FOR RESIDUAL HEAT REMOVAL SYSTEM OPERATION Parameter Value Residual heat removal system startup 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> after reactor shutdown Reactor coolant system initial pressure approximately 450 psia Reactor coolant system initial temperature approximately 350°F Component cooling water design temperature 105°F Cooldown time, hours after initiation of residual approximately 16 heat removal system operation Reactor coolant system cold temperature 140°F Decay heat generation at 20 hours2.314815e-4 days <br />0.00556 hours <br />3.306878e-5 weeks <br />7.61e-6 months <br /> after reactor 64 x 106 Btu/hr shutdown

Revision 5209/29/2016 NAPS UFSAR 5.5-59 Table 5.5-9 RESIDUAL HEAT REMOVAL SYSTEM CODES AND CLASSIFICATIONS Component Code Residual heat removal pump ASME,a Class II Residual heat exchanger Tube side ASME,Section III,b Class C Shell side ASME, Section VIIIc Piping ANSI B31.7d Valves ANSI B16.5e

a. Draft ASME Code for Pumps and Valves for Nuclear Power, November 1968.
b. ASME Code,Section III, Nuclear Vessels, 1968 Edition.
c. ASME Code,Section VIII, Pressure Vessels, 1968 Edition.
d. ANSI, B31.7, Nuclear Power Piping, 1969 Edition.
e. ANSI, B16.5, Steel Pipe Flanges and Flanged Fittings, 1968 Edition.

Revision 5209/29/2016 NAPS UFSAR 5.5-60 Table 5.5-10 RESIDUAL HEAT REMOVAL SYSTEM COMPONENT DATA Parameter Value Residual heat removal pump Number 2 Design pressure 600 psig Design temperature 400°F Design flow 4000 gpm Design head 225 ft Residual heat exchanger Number 2 Design heat removal capacity 30.5 x 106 Btu/hr Tube-side Shell-side Design pressure 600 psig 150 psig Design temperature 400°F 200°F 6

Design flow 2.0 x 10 lb/hr 4.45 x 106 lb/hr Inlet temperature 140°F 105°F Outlet temperature 123°F 113°F Material Austenitic stainless steel Carbon steel Fluid Reactor coolant Component cooling water Piping and Valves Isolation Valves Valves and Piping in and Piping the Isolated Loop Design pressure 2485 psig 600 psig Design temperature 650°F 400°F Material Austenitic stainless steel Austenitic stainless steel Pressure relief valve Valve Relief pressure 467 psig Relief capacity 900 gpm Design pressure 600 psig Design temperature 400°F Material Austenitic stainless steel

Revision 5209/29/2016 NAPS UFSAR 5.5-61 Table 5.5-11 PRESSURIZER DESIGN DATA Parameter Value Design pressure 2485 psig Design temperature 680°F Surge line nozzle diameter 14 in.

Heatup rate of pressurizer using heaters only 55°F/hr Internal volume 1400 ft3 Table 5.5-12 REACTOR COOLANT SYSTEM DESIGN PRESSURE TYPICAL SETTINGS (PSIG)

Parameter Value Design pressure 2485 Operating pressure 2235 Safety valves 2485 Power relief valves 2335 Pressurizer spray valves (begin to open) 2260 Pressurizer spray valves (full open) 2310 High-pressure trip 2360 High-pressure alarm 2335 Low-pressure trip (typical, but variable) 1870 Pressurizer power relief valve auto block and alarm 2000 (P-11)

(PORVs blocked below setpoint)

Low-low pressure safety injection 1780 Hydrostatic test pressure 3107 Backup heaters on 2210 Proportional heaters (begin to operate) 2250 Proportional heaters (full operation) 2220

Revision 5209/29/2016 NAPS UFSAR 5.5-62 Table 5.5-13 PRESSURIZER QUALITY ASSURANCE PROGRAM Examination RT UT PT MT Heads Plates Yes Cladding Yes Shell Plates Yes Cladding Yes Heaters Tubinga Yes Yes Centering of element Yes Nozzles (forgings) Yes Yesb Yesb Weldments Shell, longitudinal Yes Yes Shell, circumferential Yes Yes Cladding Yes Nozzle safe end (if forging) Yes Yes Instrument connections Yes Support skirt Yes Yes Temporary attachments after removal Yes All welds and plate heads after hydrostatic tests Yes Final assembly All accessible exterior surfaces after hydrostatic test Yes Key: RT = radiographic UT = ultrasonic PT = dye penetrant MT = magnetic particle

a. Or a UT and ET.
b. MT or PT.

Revision 5209/29/2016 NAPS UFSAR 5.5-63 Table 5.5-14 PRESSURIZER RELIEF TANK DESIGN DATA Parameter Value Design pressure 100 psig Rupture disk release pressure 100 +/- 5 psig Design temperature 340°F Total rupture disk relief capacity at 100 psig 1.6 x 106 lb/hr Table 5.5-15 REACTOR COOLANT SYSTEM BOUNDARY VALVE DESIGN PARAMETERS Parameter Value Reactor coolant loop stop valves Design/normal operating pressure 2485/2235 psig Preoperational plant hydrotest 3107 psig Design temperature 650°F Hot-leg valve size, nominal 29 in.

Cold-leg valve size, nominal 27-1/2 in.

Open/close travel time 210 sec Other reactor coolant boundary valves Design/normal operating pressure 2485/2235 psig Preoperational plant hydrotest 3107 psig Design temperature 650°F

Revision 5209/29/2016 NAPS UFSAR 5.5-64 Table 5.5-16 REACTOR COOLANT SYSTEM VALVE QUALITY ASSURANCE PROGRAM Examination RT UT PT Valves Castings Yes Yes Forgings (no UT for valves 2 in. and smaller) Yes Yes Key: RT = radiographic UT = ultrasonic PT = dye penetrant

Revision 5209/29/2016 NAPS UFSAR 5.5-65 Table 5.5-17 PRESSURIZER VALVES DESIGN PARAMETERS Parameter Value Pressurizer spray control valves Number 2 Design pressure 2485 psig Design temperature 650°F Expected flow for both valves full open 850-880 gpm Fluid temperature 547°F Pressurizer safety valves Number 3 Maximum relieving capacity (ASME rated flow), each 380,000 lb/hr Set pressure 2485 psig Fluid Saturated steam Backpressure Normal 3-5 psig Expected during discharge 350-500 psig Pressurizer power relief valves Number 2 Design pressure 2485 psig Design temperature 650°F Relieving capacity, maximum at 2335 psig, each 210,000 lb/hr Fluid Saturated steam Table 5.5-18 MAXIMUM STEAM GENERATOR AND REACTOR COOLANT PUMP FOOT LOADS (KIPS)

Component Direction Total a Steam generator Tangential 520 Vertical compression 960 Vertical tension 714 Reactor coolant pump Tangential 381 Vertical compression 1197 Vertical tension 946

a. Faulted condition, thermal + operating pressure + deadweight + SRSS of seismic (DBE) and pipe rupture.

Revision 5209/29/2016 NAPS UFSAR 5.5-66 Table 5.5-19 MAXIMUM LOAD (KIPS), SUPPORTS Concrete Reactions Loads a

From Node Direction Pipe Rupture Seismic (DBE) Normald Totalb Steam Generator 52 Z +/-685c +/-688 +/-268 1239 Supports 61 Z +/-529c +/-424 +/-387 1065 71 Y +/-461c +/-695 +/-62 896 82 Y +/-236c +/-322 +/-99 499 88 Z +/-824c +/-707 +/-148 1234 97 Z +/-615c +/-501 +/-178 971 Pump Columns 9 Z +/-362c +/-430 +/-461 1023 13 Z +/-631c +/-239 +/-227 901 16 Z +/-529c +/-264 +/-188 779

a. Refer to Figure 5.5-11.
b. Obtained by adding normal to the SRSS of pipe rupture and seismic.
c. Loads are conservatively obtained by the absolute sum of the reactions resulting from each component of force and moment applied to the support frames.
d. Deadweight + thermal + operating pressure.

Table 5.5-20 MAXIMUM LOAD (KIPS), SNUBBERS AND STRUTS Loads Pipe Seismic Concrete Reactions From Nodea Direction Normalc Totalb Rupture (DBE)

Steam Generator 110 Y +/-52 +/-644 +/-282 755 Upper Supports 112 X 0 +/-561 +/-355 664 115 Y +/-52 +/-644 +/-282 755 118 X 0 +/-561 +/-355 664

a. Refer to Figure 5.5-11.
b. Normal plus SRSS of pipe rupture and seismic.
c. Deadweight + thermal + operating pressure.

Revision 5209/29/2016 NAPS UFSAR 5.5-67 Figure 5.5-1 REACTOR COOLANT PUMP 1-RC-P-1C

Revision 5209/29/2016 NAPS UFSAR 5.5-68 Figure 5.5-2 REACTOR COOLANT PUMP 1-RC-P-1A & -1B; 2-RC-P-1A, 1B & -1C

Revision 5209/29/2016 NAPS UFSAR 5.5-69 Figure 5.5-3 REACTOR COOLANT PUMP ESTIMATED PERFORMANCE CHARACTERISTIC

Revision 5209/29/2016 NAPS UFSAR 5.5-70 Figure 5.5-4 51F SERIES STEAM GENERATOR

Figure 5.5-5 RESIDUAL HEAT REMOVAL SYSTEM Revision 5209/29/2016 NAPS UFSAR 5.5-71

Revision 5209/29/2016 NAPS UFSAR 5.5-72 Figure 5.5-6 PRESSURIZER

Revision 5209/29/2016 NAPS UFSAR 5.5-73 Figure 5.5-7 REACTOR COOLANT LOOP STOP VALVE

Revision 5209/29/2016 NAPS UFSAR 5.5-74 Figure 5.5-8 REACTOR VESSEL SUPPORT

Revision 5209/29/2016 NAPS UFSAR 5.5-75 Figure 5.5-9 STEAM GENERATOR AND REACTOR COOLANT PUMP

Figure 5.5-10 STEAM GENERATOR AND REACTOR COOLANT PUMP LOWER SUPPORT Revision 5209/29/2016 NAPS UFSAR 5.5-76

Revision 5209/29/2016 NAPS UFSAR 5.5-77 Figure 5.5-11 LOAD PATHS INTO REINFORCED CONCRETE

Revision 5209/29/2016 NAPS UFSAR 5.5-78 Figure 5.5-12 (SHEET 1 OF 2)

PRESSURIZER SUPPORT

Revision 5209/29/2016 NAPS UFSAR 5.5-79 Figure 5.5-12 (SHEET 2 OF 2)

PRESSURIZER SUPPORT

Figure 5.5-13 (SHEET 1 OF 2)

DYNAMIC MODEL OF STEAM GENERATOR AND PUMP SUPPORTS Revision 5209/29/2016 NAPS UFSAR 5.5-80

Figure 5.5-13 (SHEET 2 OF 2)

DYNAMIC MODEL OF STEAM GENERATOR AND PUMP SUPPORTS Revision 5209/29/2016 NAPS UFSAR 5.5-81

Figure 5.5-14 STEAM GENERATOR-PUMP SUPPORTS STRESS MODEL Revision 5209/29/2016 NAPS UFSAR 5.5-82

Figure 5.5-15 DYNAMIC MODEL FOR PRESSURIZER SUPPORTS Revision 5209/29/2016 NAPS UFSAR 5.5-83

Figure 5.5-16 DYNAMIC MODEL FOR REACTOR VESSEL SUPPORTS Revision 5209/29/2016 NAPS UFSAR 5.5-84

Revision 5209/29/2016 NAPS UFSAR 5.5-85 Figure 5.5-17 TEMPERATURE DISTRIBUTION IN SNUBBER ASSEMBLY BETWEEN STEAM GENERATOR SUPPORT AND REACTOR COOLANT PUMP SUPPORTCASE 1, 105°F AMBIENT Note: Internal design details of the installed snubbers may differ slightly from the details shown above.

Revision 5209/29/2016 NAPS UFSAR 5.5-86 Figure 5.5-18 TEMPERATURE DISTRIBUTION IN SNUBBER ASSEMBLY BETWEEN STEAM GENERATOR SUPPORT AND REACTOR COOLANT PUMP SUPPORTCASE 1, 70°F AMBIENT Note: Internal design details of the installed snubbers may differ slightly from the details shown above.

Figure 5.5-19 TEMPERATURE DISTRIBUTION IN SNUBBER ASSEMBLY BETWEEN STEAM GENERATOR SUPPORT AND CONCRETE WALLSCASE 2, 105°F AMBIENT Revision 5209/29/2016 Note: Internal design details of the installed snubbers may differ slightly from the details shown above.

NAPS UFSAR 5.5-87

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Revision 5209/29/2016 NAPS UFSAR 5.6-1 5.6 INSTRUMENTATION APPLICATION 5.6.1 Design Bases Process control instrumentation is provided to acquire data on the pressurizer and on a per-loop basis for the key process parameters of the reactor coolant system (Figure 5.6-1)

(including the reactor coolant pump motors), as well as for the residual heat removal system. The pick-off points for the reactor coolant system are shown in Reference Drawings 1 and 2, and for the residual heat removal system in Reference Drawing 3. In addition to providing input signals for the protection system and the plant control systems, the instrumentation sensors furnish input signals for monitoring and/or alarming purposes for the following parameters:

1. Temperatures.
2. Flows.
3. Pressures.
4. Water levels.

In general, these input signals are used for the following purposes:

1. Provide input to the reactor trip system for reactor trips as follows:
a. Overtemperature delta T.
b. Overpower delta T.
c. Low pressurizer pressure.
d. High pressurizer pressure.
e. High pressurizer water level.
f. Low primary coolant flow.
2. Provide input to the engineered safety features actuation system as follows:
a. Pressurizer low-low pressure.
b. High differential pressure between any steam line and the other steam lines.
c. High steam flow coincident with low-low Tavg or low steam-line pressure.
3. Furnish input signals to the non-safety-related systems, such as the plant control systems and surveillance circuits so that:
a. Reactor coolant average temperature (Tavg) will be maintained within prescribed limits.

The resistance temperature detector instrumentation is identified in Reference Drawing 1.

b. Pressurizer level control, using Tavg control, will maintain the coolant level within prescribed limits.

Revision 5209/29/2016 NAPS UFSAR 5.6-2

c. Pressurizer pressure will be controlled within specified limits.
d. Steam dump control, using Tavg control, will accommodate excess power generation.
e. Information is furnished to the control room operator and at local stations for monitoring.

Instrumentation necessary to monitor the reactor vessel level and to detect conditions of inadequate core cooling is provided by the reactor vessel level indication system which is described in Section 7.9.2.2.

The following is a functional description of the process control instrumentation of the system. Unless otherwise stated, all indicators, recorders, and alarm annunciators are located in the main control room.

5.6.2 Description 5.6.2.1 Temperature Measuring Instrumentation

1. Resistance Temperature Detectors (Narrow Range)

Three thermowell mounted resistance temperature detectors, for the reactor protection and control, are installed in the hot leg scoops of each loop near the inlet to the steam generator.

The scoops are 120 degrees apart in the cross-sectional plane of the reactor coolant leg, and extend into the pipe to sample the flow.

One thermowell mounted resistance temperature detector, for reactor protection and control, is installed in the cold leg nozzle of each loop at the discharge of the reactor coolant pump.

Signals from these instruments are used to compute the reactor coolant delta T (temperature of the hot leg, Thot, minus the temperature of the cold leg, Tcold) and an average reactor coolant temperature (Tavg). The Tavg and T for each loop is indicated on the main control board.

2. Cold-Leg and Hot-Leg Temperatures (Wide Range)

Temperature detectors, located in the thermometer wells in the cold and hot-leg piping of each loop, supply signals to wide-range temperature recorders. This information is used by the operator to control coolant temperature during start-up and shutdown.

As a result of IE Bulletin 79-27, Loss of Non-Class 1E Instrumentation and Control Power System Bus during Operation, the original design basis for supplying power to the wide-range cold-leg and hot-leg temperature loops was modified. In the original design, all cold-leg temperature loops were supplied by one vital bus and all hot-leg temperature loops by the other. In the present design, the vital buses are realigned so that the associated hot-leg temperature loop and cold-leg temperature loop of the same loop are supplied by the same vital bus which is different than that aligned for one of the other two loops. The modification allows the operator to verify natural circulation by the use of the differential temperature

Revision 5209/29/2016 NAPS UFSAR 5.6-3 between Thot and Tcold on at least two reactor coolant loops in the event of loss of the reactor coolant pumps and one vital bus. Two hot-leg temperature indications are available at the auxiliary monitoring panel. One of them is installed with a specific separation from the additional temperature indication available in the control room. This separation meets 10 CFR 50 Appendix R Section III.G.2.

3. Pressurizer Temperature There are three temperature detectors in the pressurizer, one in the steam phase and two in the water phase. All detectors supply signals to temperature indicators and high-temperature alarms. The steam-phase detector, located near the top of the vessel, is used during start-up to determine water temperature when the pressurizer is completely filled with water. The water-phase detectors, located at an elevation near the center of the heaters, are used during cooldown when the steam-phase detector response is slow because of poor heat transfer.
4. Surge Line Temperature This detector supplies a signal for a temperature indicator and a low-temperature alarm. Low temperature is an indication that the continuous spray rate is too small.
5. Safety and Relief Valve Discharge Temperatures Temperatures in the pressurizer safety and relief valve discharge lines are measured and indicated. An increase in a discharge line is an indication of leakage through the associated valve.
6. Spray Line Temperatures Temperatures in the spray lines from two loops are measured and indicated. Alarms from these signals are actuated by low spray water temperature. Alarm conditions indicate insufficient flow in the spray lines.
7. Pressurizer Relief Tank Water Temperature The temperature of the water in the pressurizer relief tank is indicated and an alarm actuated by high temperature informs the operator that cooling of the tank contents is required.
8. Reactor Vessel Flange Leakoff Temperature The temperature in the leakoff line from the reactor vessel flange o-ring seal leakage monitor connections is indicated. An increase in temperature above ambient is an indication of o-ring seal leakage. High temperature actuates an alarm.
9. Reactor Coolant Pump Motor Temperature Instrumentation
a. Upper and Lower Thrust Bearing Shoes Temperature

Revision 5209/29/2016 NAPS UFSAR 5.6-4 Resistance temperature detectors are located in the shoes of upper and lower thrust bearings. These elements provide a signal high-temperature alarm and recorder input.

b. Stator Winding Temperature The stator windings contain six resistance-type detectors, two, per phase, imbedded in the windings. A signal from one of these detectors actuates a high-temperature alarm and recorder input.
c. Upper and Lower Bearing Temperature Resistance temperature detectors are located in the upper and lower radial bearings.

Signals from these detectors actuate a high-temperature alarm and recorder input.

5.6.2.2 Flow Indication Reactor Coolant Loop Flow Rates Flow in each reactor coolant loop is monitored by three differential-pressure measurements at a piping elbow tap in each reactor coolant loop. These measurements on a two-out-of-three coincidence circuit provide a low-flow signal to actuate a reactor trip above specified power levels.

5.6.2.3 Pressure Indication

1. Pressurizer Pressure The pressurizer is equipped with multiple transmitters used to sense reactor coolant pressure.

Three transmitters provide inputs to the protection circuits. Two additional transmitters are used in the control of reactor pressure.

The protection related pressure transmitters provide signals for individual indicators in the control room and to the reactor protection system for actuation of both the low pressure and high pressure trip. In addition, these transmitters provide an input to the low pressure safety injection actuation logic circuits, and provide the input for P-11, that allows the manual block of the safety injection actuation signals and blocks automatic operation of the power-operated relief valves. More detail on these functions is provided in Sections 7.2 and 7.3.

One of the control transmitters is used in conjunction with a reference pressure to develop a demand signal for controllers providing for pressurizer proportional heater control, pressurizer backup heater control, spray valve control, and control of one of two PORVs.

This transmitter also provides control room indication, alarms, and an input to a strip chart recorder. An additional output from this transmitter is provided at the auxiliary monitoring panel and is installed with a specific separation from the pressurizer pressure indication available in the control room. This separation meets 10 CFR 50 Appendix R Section III.G.2.

Revision 5209/29/2016 NAPS UFSAR 5.6-5 The other control transmitter provides input to the second PORV and provides control room indication, alarms, and input to a strip chart recorder. More detail on the pressure control function is found in Section 7.7.1.5.

2. Reactor Coolant Reference Pressure (Deadweight Test)

A differential-pressure transmitter provides a signal for the indication of the difference between the pressurizer pressure and a pressure generated by a deadweight tester located outside the reactor containment. The indication is used for online calibration checks of the pressurizer pressure signals.

3. Reactor Coolant Loop Pressures Three wide-range pressure transmitters are located on two of the hot legs. Two of these wide-range transmitters provide pressure indication over the full operating range and serve as a guide to the operator for manual pressurizer heater and spray control and letdown to the Chemical and Volume Control System during plant start-up and shutdown. The third wide-range pressure transmitter and one of the above mentioned transmitters are used during the low temperature solid water phase of reactor coolant system pressurization to automatically actuate the pressurizer PORV if undesirable temperature and pressure conditions develop.

The two wide-range channels provide the permissive signals for the residual heat removal loop suction line isolation valve interlock circuit.

There are also two local pressure indicators for operator reference during the shutdown condition, which are located in two of the hot loops.

4. Pressurizer Relief Tank Pressure The pressurizer relief tank pressure transmitter provides a signal for indication and high pressure alarm.
5. Reactor Coolant Pump Motor Oil Pressure
a. Oil Lift Switch A dual-purpose switch is provided on the high-pressure oil lift system. The switch is part of an interlock system that will prevent the starting of the reactor coolant pump until the oil lift pump is started manually and the oil pressure is adequate to permit starting the RCP. In addition, the switch provides indication on the main control board that the lift oil pressure has reached sufficient pressure to allow starting of the reactor coolant pump. The oil lift pump is stopped manually after the reactor coolant pump is operating. A local pressure gauge is also provided.

Revision 5209/29/2016 NAPS UFSAR 5.6-6

b. Lower Oil Reservoir Liquid Level A level switch is provided in the motor lower radial bearing oil reservoir. The switch will actuate a high and low-level alarm on the main control board.

Note: The lower bearing oil high level alarms to the Main Control Room have been disconnected.

c. Upper Oil Reservoir Liquid Level A level switch is provided in the motor upper radial bearing and thrust bearing oil reservoir. The switch will actuate a high- or low-level alarm on the main control board.

5.6.2.4 Liquid Level Indication

1. Pressurizer Level Three pressurizer liquid level transmitters provide signals for use in the reactor control and protection system, the emergency core cooling system, and the Chemical and Volume Control System. Each transmitter provides an independent high-water-level signal that is used to actuate an alarm and a reactor trip. The transmitters also provide independent low-water-level signals that will activate an alarm. Each transmitter also provides a signal for a level indicator located on the main control board.

In addition to the above, signals may be selected for specific functions as follows:

a. Any one of the three level transmitters may be selected by the operator for display on a level recorder located on the main control board. This same recorder is used to display a pressurizer reference liquid level.
b. Two of the three transmitters perform the following function (a) selector switch allows the third transmitter to replace either of these two:

(1) One transmitter provides a signal that will actuate an alarm when the liquid level falls to a fixed level setpoint. The same signal will trip the pressurizer heaters off and close the letdown line isolation valves.

(2) One transmitter supplies a signal to the liquid level controller for charging flow control and also initiation of a low-flow (high demand) alarm. This signal is also compared to the reference level and actuates a high-level alarm and turns on all pressurizer backup heaters if the actual level exceeds the reference level. If the actual level is lower than the reference level, a low alarm is actuated.

A signal is also transmitted to the auxiliary monitoring panel and a pressurizer water level indication is installed with a specific separation from the indicator available in the control room. This separation meets 10 CFR 50 Appendix R Section III.G.2.

Revision 5209/29/2016 NAPS UFSAR 5.6-7 A fourth independent pressurizer level transmitter, calibrated for low temperature conditions, provides water level indication during start-up, shutdown, and refueling operations.

2. Pressurizer Relief Tank Level The pressurizer relief tank level transmitter supplies a signal for an indicator and high and low-level alarms.

5.6.3 Evaluation The reactor coolant system design and operating pressure, together with the safety, power relief and pressurizer spray valve setpoints, and the protection system setpoint pressures, are listed in Table 5.5-12. The design pressure allows for operating transient pressure changes. The selected design margin considers core thermal lag, coolant transport times and pressure drops, instrumentation and control response characteristics, and system relief valve characteristics.

Process control instrumentation for the residual heat removal system is provided for the following purposes:

1. Furnish input signals for monitoring and/or alarming purposes for:
a. Temperature indications.
b. Pressure indications.
c. Flow indications.
2. Furnish input signals for control purposes of such processes as:
a. Residual heat removal inlet valves control circuitry. See Section 7.6.2 for the description of the interlocks and requirements for automatic closure.
b. Control valve in the residual heat removal heat exchanger bypass\ line to control temperature of reactor coolant returning to reactor coolant loops during plant cooldown.

Revision 5209/29/2016 NAPS UFSAR 5.6-8 5.6 REFERENCE DRAWINGS The list of Station Drawings below is provided for information only. The referenced drawings are not part of the UFSAR. This is not intended to be a complete listing of all Station Drawings referenced from this section of the UFSAR. The contents of Station Drawings are controlled by station procedure.

Drawing Number Description

1. 11715-FM-093A Flow/Valve Operating Numbers Diagram: Reactor Coolant System; Loops 1, 2, & 3; Unit 1 12050-FM-093A Flow/Valve Operating Numbers Diagram: Reactor Coolant System; Loops 1, 2, & 3; Unit 2
2. 11715-FM-093B Flow/Valve Operating Numbers Diagram: Reactor Coolant System, Unit 1 12050-FM-093B Flow/Valve Operating Numbers Diagram: Reactor Coolant System, Unit 2
3. 11715-FM-094A Flow/Valve Operating Numbers Diagram: Residual Heat Removal System, Unit 1 12050-FM-094A Flow/Valve Operating Numbers Diagram: Residual Heat Removal System, Unit 2

Figure 5.6-1 REACTOR COOLANT SYSTEM PROCESS CONTROL INSTRUMENTATION Revision 5209/29/2016 NAPS UFSAR 5.6-9

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Revision 5209/29/2016 NAPS UFSAR 5A-i Appendix 5A1 Discussion Between the Nuclear Regulatory Commission and Virginia Electric & Power Company on Steam Generator Lower and Reactor Coolant Pump Supports for North Anna Units No. 1 and 2

1. Appendix 5A: Discussion between the Nuclear Regulatory Commission and Virginia Electric & Power Company on Steam Generator Lower and Reactor Coolant Pump Supports for North Anna Units No.1 and 2, Transcript, dated April 13, 1976; corrected copy of transcript, dated May 18, 1976; 164 pages, which were taken from original report and are not subject to revision.

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Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-1 ATTACHMENT 1 TO APPENDIX 5A NRC QUESTIONS AND VEPCO RESPONSES SUBSEQUENT TO THE VEPCO PRESENTATION OF APRIL 13, 1976 Because Appendix 5A is a transcript of a meeting, the responses to NRC questions relating to that meeting cannot be merged into Appendix 5A itself. Consequently, these comments and their responses are attached as originally submitted.

Question 1 For each postulated break location in the reactor coolant system, identify the location, state the flow area (sq. in.), provide a sketch of the associated pipe restraint, and discuss the direction and envelope of pipe motion. If different break areas at any location have been used for certain analysis, indicate the alternative break areas used, the analysis in which they were used, and the basis for selecting the alternative break area.

Response

See Table 1.

Question 2 Supplement VEPCOs April 13, 1976, presentation regarding the steam generator lower support and the reactor coolant pump support with the following information:

1. Provide design allowable stress limits used in the Z short transverse direction for normal, upset and faulted conditions. Provide the actual calculated maximum stresses in this direction for the normal, upset and faulted conditions and demonstrate that these values have included residual stresses.
2. Dr. Corten indicated that his fracture toughness calculation assumed a through thickness allowable stress of approximately 17 ksi. Dr. Goldstein indicated the current code allowable stresses in this direction are approximately 20 ksi. Confirm that there are no operating stresses in the through thickness direction greater than 17 ksi.
3. Describe the postulated pipe break identified by number in summary tables Comparison of Maximum Beam Stresses to Design Criteria and Through Transverse Stresses at Member Correction Welds (i.e., Break Nos. 7, 4, 2, 12). Also provide the break flow area used in these analyses.

Response

1. Normal, upset, and faulted condition allowable stress limits, as defined in ASME III, Subsection NF, are not applicable to the design of the steam generator lower supports and the reactor coolant pump supports for North Anna Units 1 and 2, since the design of these

Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-2 supports preceded the first issue of ASME III, Subsection NF by several years. Further, the design criteria used for these supports did not require any reduction in allowable tension stress limits in the short transverse (Z) direction.

The design criteria used for the North Anna Units 1 and 2 steam generator lower and reactor coolant pump supports combined the effects of dead weight, design-basis earthquake, and pipe rupture loads for the design condition. This load combination is equivalent to the faulted condition of ASME III, Subsection NF, for current designs. Since the design condition used for the North Anna supports resulted in maximum calculated stresses which, in turn, were compared to and found to be below a conservative allowable stress (0.9 x yield), no analysis was performed for lesser combinations of loads, such as operating-basis earthquake, which would be equivalent to the upset condition of ASME III, Subsection NF. However, for comparison purposes, the allowable primary tension stress limits in the short transverse (Z) direction, provided in ASME III, Subsection NF, are as follows:

Short Transverse (Z)

Condition Material Allowable Stress, ksi Normal SA-36 10.8 Upset 10.8 Faulted 20.3 Normal SA-572 12.6 Upset 12.6 Faulted 21.0 If operating condition stresses had been calculated in the original design, they would have been compared to a working stress allowable of 0.6 x yield. Even for the faulted condition, the short transverse stresses are below this value.

However, again for comparison purposes, for the North Anna supports, the maximum calculated stresses in the short transverse direction occur in A-36 material and are:

Normal - 3.00 ksi Upset - 8.82 ksi Faulted - 12.54 ksi The above normal and upset condition stresses include the effects of thermal and pressure loop expansion loads and are conservatively added to the stress summation for comparison to primary stress allowables. The current ASME III Code (NF 3231.1) permits an allowable base of three times the primary stress limit when such secondary effects are considered, since such loads are self-limiting.

Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-3 Past and current industry practice does not include residual stresses in these values.

Unquantified stresses, such as residual stresses, are accounted for in the codes when working allowable stresses are established. Indeed, it would be counter to good engineering practice for the designer to add residual stresses to primary stresses in establishment of the size of members. Such stresses are self-limiting in character, and if they were to be considered, they would be comparable to free-end displacement type stresses (ASME III, NF-3231.1) and as such would be compared to an allowable of three times the primary tensile stress limit when combined with mechanical loads for the normal and upset conditions (ASME III, NF-3231.1).

2. As shown in the response to Question 2, Item 1 above, operating condition stresses in the through thickness direction are substantially less than the 17 ksi used by Dr. Corten in his fracture toughness calculations.
3. The area of the pipe breaks used to derive the forcing functions applied to the support members mentioned in the summary tables is mentioned below:

Break Number Location of Break Type of Break Break Opening Area (ft2) 2 RPV inlet nozzle Guillotine 4.125 4 Steam generator Guillotine 5.24 nozzle 7 Steam generator inlet Split 4.9086 elbow on the intrados 12 Loop closure weld in Guillotine 5.24 crossover leg Question 3 Regarding the North Anna Units 1 and 2 steam generator and pump support members, provide the following information:

1. The specifications and supplementary requirements, if any, to which the materials were ordered.
2. The size and shapes of material ordered.
3. The number of suppliers involved.
4. The number of heats of material used.
5. The status of heat traceability maintained during fabrication and repair.
6. A summary of actual mechanical and chemical test data (from material certifications) for all heats of material used in fabrication.

Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-4

Response

All main welded members on the North Anna Units 1 and 2 steam generator lower and reactor coolant pump supports are structural shapes of the wide-flange beam type. Based on material certification data provided by the fabricator:

1. The ASTM material specifications to which the members were procured are:
a. ASTM A 36-69, Standard Specification for Structural Steel.
b. ASTM A 572-68, Standard Specification for High-Strength Low-Alloy Columbium-Vanadium Steels of Structural Quality.

During repair of the Unit 1 steam generator lower supports, certain welded sub-assemblies were prefabricated and used to replace portions of the original materials. In these prefabricated sub-assemblies, some ASTM A 572-70A material was utilized for reasons of availability.

Ultrasonic inspection of material 3 in. or greater in thickness was specified as a supplemental requirement.

2. The size and shape designations for the members:

W14 x 605.

W14 x 426.

W14 x 176 (reactor coolant pump supports only).

W14 x 142 (steam generator lower supports only).

3. Bethlehem Steel Corporation supplied the members used in the original fabrication and repair of the support structures.
4. The members used in fabrication and repair of the support structures are comprised of 20 heats of materials, as shown on Tables 2, 3, 4 and 5.
5. Although not required by contract, the original fabricator provided partial material traceability by marking each material certification with information regarding the type of support, unit (North Anna 1 and 2), and fabrication piece number. The small quantity of repair members (see Response to Question 3, Item 1, above) were physically marked for identification.
6. A summary of mechanical and chemical test data from the mill certifications for the members in the supports is contained on Tables 2, 3, 4 and 5.

A detailed review of chemical analysis and hardness tests performed on the Unit 2 Cubicle C Reactor Coolant Pump support back weldment revealed two W14 x 176 lb vertical support members conforming to the chemical and physical requirements of ASTM A242, Type 1.

Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-5 The specific material test data are listed in Table 6. An evaluation of the operating temperatures for these supports in conjunction with the mechanical properties demonstrates that the material possesses adequate toughness for the application.

Question 4 Regarding the longitudinal CVN data reported for four heats of A-36 steel used in the supports, provide the following information:

1. The size and shape material from which specimens were removed.
2. If sufficient test material is available, provide CVN values in the short-transverse direction for these heats of material. Three specimens from each heat at 80°F and at 125°F are considered adequate for this purpose.
3. If test material is available from other heats used in fabrication of the supports, provide additional CVN data in both longitudinal and short transverse direction to increase the fracture toughness data base for these materials.

Response

1. The four original samples charpy tested by VEPCO and reported to the NRC were designated AB, CD, F2A, and W96. A complete description of these materials is found in Table 7.
2. The four original samples of material were charpy V-notch tested at 80°F and 125°F in the short transverse direction (through thickness direction) to supplement the information obtained by the longitudinal direction testing that was previously provided to the NRC.

Three specimens from each sample were tested at 80°F and three from each sample at 125°F.

The results are presented in Table 8.

3. The criteria applied to establish the availability of base metal from the supports for testing are: (1) the material must represent a primary load carrying member, (2) the material must be traceable to that portion of a structure from which it was removed to allow correlation to a known piece number(s) and thereby a heat number(s), and (3) the sample must be large enough and thick enough to obtain specimens for testing that would produce meaningful data.

An analysis of the scrap material available from both Unit 1 and Unit 2 structures has shown the only material that will satisfy the criteria stated above are the ASTM A-36 W14 x 426 lb beams from pieces 21 through 26 of the Unit 1 steam generator structures. Further analysis has shown that three heats of the 426 lb beams were used for these six piece numbers in all six steam generator cubicles (Units 1 and 2). The three available heats are 182C535, 182C174, and 171C866, and as shown in response to Question 4, Item 1 above, at least two of these heats have been tested previously. Only nine heats (total) of ASTM A36 W14 x 426 beams were used in all six steam generator and all six RC pump structures.

Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-6 The three heats available for testing represent over 30 percent of the total linear feet of 426 lb beams in all structures. The 426 lb beams are significant for test purposes as they are the primary load carrying beams in the steam generator support structures, and represented the second largest footage of load carrying beams in the RC pump structures (being second only to the smaller ASTM A-36 W14 x 176 beams). As noted in response to Question 4, Item 5 above, traceability of heats is to piece number(s); further identification of individual heats must be by chemical analysis. A review of the chemical analyses of the three heats available for charpy testing has shown that heat 182C535 can be identified; however, heats 182C174 and 171C866 cannot be separated one from the other by chemical analysis techniques.

To provide a higher probability that some samples of both heats 182C174 and 171C866 were tested, VEPCO has taken base metal samples for charpy tests from 11 additional identifiable locations (piece number 21 through 26) as represented by scrap pieces of 426 lb beams from the Unit 1 steam generator supports. Chemical analysis of these samples shows two to be heat 182C535, eight to represent heat 182C174 and/or 171C866, and one sample to be one of three heats. Charpy testing was accomplished in both the longitudinal- and short- transverse directions at test temperatures of 80°F and 125°F. Three charpy specimens were tested in both directions at both temperatures making a total of 12 charpy specimens per sample tested. The specific data is presented in Table 9.

Question 5 Regarding the two core samples removed from North Anna Unit 2 support weldments that reportedly showed evidence of lammellar tearing, state whether the weldments in question were subjected to ultrasonic examination prior to the core sample removal and provide the test results, if any.

Response

The welds were not subjected to ultrasonic examination prior to core sample removal because the ultrasonic examination of selected high stress welds was not performed until all examinations by the magnetic particle (MT) method had been successfully completed. The core samples were removed during the MT examinations and the cavities caused by such samples were subsequently weld repaired and subjected to MT examination. The two welds that were completed and repaired were not included in the group of welds selected for ultrasonic examination because they were not designated as high stressed welds.

Question 6 Provide the results of your review of the consequences of lower support member failure(s) going from several members to the entire structure, for the steam generator supports.

Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-7

Response

The April 13, 1976 presentation described the results of an analysis that arbitrarily disabled one full interior corner of the steam generator support frame. The load/stress redistribution exhibited was intended to amplify the redundant nature of the structure. More detailed stress summaries for the disabled corner example in the same format as the response to Question 7 are provided in Table 10.

It is important to note that this review was intended to emphasize a characteristic of these structures, not to chart a potential progression of structural failure, beam by beam. Nor was it necessary to apply rigorous analysis methods for any one or all possible sequence or combinations of arbitrary member failures. Given the number of beams, the number of loading conditions, and the time varying nature of the loads, any effort to evaluate such a progression would very quickly become unphysical because the input load/displacements are based upon an integral system dynamic analysis. Further, the number of possible permutations in terms of order of failure are extremely large. A permutation calculation indicates more than 5000 such sequences for a single seven element interior corner section. This such number, for the first corner only, is a minimum, since many more of the 100 or so elements of the frame are involved in such an evaluation (1001 sequences) before the entire structure can be considered to have failed.

In summary, such an analysis, were it to be performed, would not provide any meaningful results. As VEPCO demonstrated in the April 13, 1976 presentation, the North Anna supports were designed and repaired in accordance with all applicable design criteria, and with the modifications described in Section 5.5.9, they will safely perform their intended function. This is further illustrated by the stress levels provided in the response to Question 7. It is also shown that the supports compare favorably with even the latest applicable criteria for nuclear supports.

Question 7 Provide a stress summary for each of the steam generator lower support members and reactor coolant pump lower support members due to static, seismic (design-basis earthquake and operating-basis earthquake), and controlling loss-of-coolant accident (LOCA) cases loadings and the method of stress combination.

Response

Stress summaries for higher stressed members of both steam generator lower, and reactor coolant pump supports are provided in Table 11. Dead weight, seismic, and controlling LOCA (for each member) are given. As indicated in our response to Question 2, no analysis was performed for lesser combinations of loads, such as operating-basis earthquake, which would be equivalent to the upset condition of ASME III, Subsection NF. Stresses due to operating-basis earthquake, however, would be equal to approximately 90% of design-basis earthquake stresses,

Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-8 indicated in Tables 10 and 11, based on a comparison of component interfaces loads developed from displacement data supplied by Westinghouse.

Since these supports consist of in the excess of 150 individual members, a computer stress tabulation of all members for all load cases was not maintained. Rather a procedure was used to isolate members whose nominal stress values exceed defined screening limits for each load type.

Members below this screening limit met the design allowables with conservative margin and were not tabulated in order to reduce the size of the data base requiring more rigorous evaluation. The members identified in Table 11 by footnotes a, b, c, d, and e required a more detailed evaluation than the very conservative envelope approach.

Stress summaries were generally performed conservatively by absolute summation of maximum element stresses without regard to location in the member. When this very conservative envelope approach did not document adequate design margin, stresses were added by considering summations at consistent locations in the members as indicated in Table 11.

The purpose of the first stress summation in the stress review procedure is to eliminate from subsequent, more vigorous review as many members as possible with a minimal amount of data collection and tabulation through a number of conservative simplifications. The initial summation consists of the worst end seismic and deadweight stresses and one maximum and one minimum (enveloped) LOCA stress chosen from the maximum and minimum LOCA stresses due to all LOCAs under consideration. The enveloped LOCA stress at each member end is summed with the worst end seismic and deadweight stresses without regard to member cross-sectional quadrant, and those members exceeding stress screening limits are subjected to a second more rigorous stress summation. This second summation combines consistent (non-enveloped) LOCA stresses and seismic and deadweight stresses at each member end.

Table 1 REACTOR COOLANT SYSTEM BREAK LOCATIONS AND SITE FOR FSAR ANALYSES Justification of Break Type and Justification of Analysis Analysis Break Type Break Location (s) Break Size Location Break Size Reference Containment Guillotine RPV nozzle inlet 1188 in.2 WCAP 8172 Section 6.2.1.3.1 Section 6.2.1.1 pressure and Revision 5209/29/2016 temperature analysis RPV nozzle outlet 1320 in.2 WCAP 8172 Section 6.2.1.3.1 Section 6.2.1.1 Steam generator Single ended Hot leg 660 in.2 WCAP 8172 Section 6.2.1.1.2 Section 6.2.1 subcompartment split pressure analysis Single ended Hot leg 660 in.2 WCAP 8172 Section 6.2.1.1.2 Section 6.2.1.3.2 split Section 6.2.1.1.2.2 Reactor cavity Limited RPV nozzle outlet 178 in.2 Section 6.2.1.1.2 Section 6.2.1.1.2 Section 6.2.1.3.2 subcompartment displacement WCAP 8172 Section 6.2.1.1.2.2 pressure analysis guillotine RPV nozzle outlet 150 in.2 Section 6.2.1.3.2 Section 5A.4.6 Section 6.2.1.3.2 WCAP 8172 NAPS UFSAR 5A Att. 1-9

Table 1 (continued)

REACTOR COOLANT SYSTEM BREAK LOCATIONS AND SITE FOR FSAR ANALYSES Justification of Break Type and Justification of Analysis Analysis Break Type Break Location (s) Break Size Location Break Size Reference Pressurizer Guillotine Spray line 18.6 in.2 Section 3A.32 a Section 6.2.1 subcompartment analysis Revision 5209/29/2016 Surge line 197 in.2 Section 3A.32 a Section 6.2.1 Surge line 197 in.2 Section 3A.32 a Section 6.2.1.3.2 Section 6.2.1.1.2.2 RPV support Limited RPV nozzle 178 in.2 WCAP 8172 Section 6.2.1.1.2 Appendix 5A analysis displacement outletb guillotine RPV nozzle inletc 144 in.2 WCAP 8172 Section 5A.4.6 Appendix 5A Guillotine Cold leg break - W to provide WCAP 8236 and WCAP 8236 and Section 5A.9 outside biological Section 5A.9 Section 5A.9 shieldd ECCS analysis Guillotine Cold leg break DECLG with WCAP 8573 NP WCAP 8573 NP Section 15.4.1 (large break) discharge coefficients of 1.0, 0.6 NAPS UFSAR and 0.4

a. Largest break postulated in that particular pipe.
b. This break is used to calculate asymmetric pressure loading on RPV.
c. This break is used to calculate RPV internals loading.
d. This break is used to calculate fuel assembly hydraulic forcing functions.

5A Att. 1-10

Table 1 (continued)

REACTOR COOLANT SYSTEM BREAK LOCATIONS AND SITE FOR FSAR ANALYSES Justification of Break Type and Justification of Analysis Analysis Break Type Break Location (s) Break Size Location Break Size Reference ECCS analysis Small break Cold leg break 3, 4 and 6 in. WCAP 8356 NP WCAP 8356 NP Section 15.3.1 (small break) equivalent diameter Revision 5209/29/2016 Containment Guillotine Pump suction 1510 in.2 Section 6.2.1.3.1 Section 6.2.1.3.1 Section 6.2.1.3.1 pressure and Surge line 197 in.2 Section 6.2.1.3.1 Section 6.2.1.3.1 Section 6.2.1.3.1 temperature analyses RPV nozzle inlet 1188 in.2 Section 6.2.1 Section 6.2.1 Section 6.2.1 Pump suction 1510 in.2 Section 6.2.1 Section 6.2.1 Section 6.2.1 RPV nozzle outlet 1320 in.2 Section 6.2.1 Section 6.2.1 Section 6.2.1

.6 guillotine RPV nozzle outlet 792 in.2 Section 6.2.1 Section 6.2.1 Section 6.2.1

.326 guillotine RPV nozzle outlet 430 in.2 Section 6.2.1 Section 6.2.1 Section 6.2.1 NAPS UFSAR 5A Att. 1-11

Table 2 STEAM GENERATOR LOWER SUPPORTS - UNIT 1 HEATS OF MATERIAL Elongation Percent Reducti Heat Yield Tensile on in Hardness Description Materiala Number Point Strength Percent In. Area BHN Bend C Mn P S Si V N W 14 x 605 A 171C560 60,000 88,500 24.5 2 58.6 187 OK .19 1.04 .019 .033 .23 .07 .007 Revision 5209/29/2016 W 14 x 605 A 182C087 58,500 84,500 25.0 2 62.3 156 OK .20 1.20 .016 .021 .22 .07 .011 W 14 x 605 A 172C497 56,500 83,500 24.5 8 58.1 163 OK .21 1.17 .015 .029 .22 .06 .008 W 14 x 605 A 123C349 63,000 91,500 25.0 8 62.6 187 OK .18 1.18 .008 .012 .20 .07 .015 W 14 x 426 B 171C871 44,280 70,316 28.1 8 53.7 156 OK .21 1.15 .011 .020 .05 W 14 x 426 B 171C866 44,331 72,733 28.0 8 51.5 156 OK .24 1.11 .016 .019 .05 W 14 x 426 B 182C174 46,493 76,296 27.9 8 52.9 163 OK .21 1.13 .012 .018 .04 W 14 x 426 B 182C172 42,598 70,868 29.2 8 49.8 170 OK .24 1.16 .015 .020 .05 W 14 x 426 B 182C159 44,924 74,290 29.3 8 60.9 163 OK .26 1.20 .011 .022 .06 W 14 x 426 B 182C178 43,853 72,418 28.9 8 57.3 163 OK .24 1.19 .013 .021 .04 W 14 x 426 B 182C535 40,471 67,645 30.5 8 54.9 149 OK .22 1.10 .014 .031 .03 W 14 x 426 B 172C586 43,839 70,921 29.0 8 56.5 163 OK .20 1.15 .012 .018 .05 W 14 x 426 C 517J1106 50,980 76,000 22.0 8 OK .18 1.16 .009 .020 .03 .085 .008 W 14 x 426 C 517J1058 61,690 85,010 20.0 8 OK .21 1.20 .005 .016 .03 .097 .013 W 14 x 426 B 181C686 54,846 79,233 21.0 8 51.1 179 OK .18 1.06 .011 .023 .14 NAPS UFSAR W 14 x 426 B 182C150 47,440 75,883 27.5 8 45.3 143 OK .24 .81 .011 .023 .08

a. Material A - ASTM A572-68 Grade 42 Ty 4 KLD, stress relieved at 1,100°F furnace cooled.

Material B - ASTM A36-69, stress relieved at 1,100°F furnace cooled Material C - ASTM - A572-70A GR50A (repair replacement members) 5A Att. 1-12

Table 3 STEAM GENERATOR LOWER SUPPORTS - UNIT 2 HEATS OF MATERIAL Elongation Percent Heat Yield Tensile Reduction Hardness Description Materiala Number Point Strength Percent In. in Area BHN Bend C Mn P S Si V N W 14 x 605 A 182C087 b W 14 x 605 A 123C349 b Revision 5209/29/2016 W 14 x 605 A 171C560 b W 14 x 605 A 172C497 b W 14 x 426 B 171C866 b W 14 x 426 B 171C871 b W 14 x 426 B 182C172 b W 14 x 426 B 182C174 b W 14 x 426 B 182C178 b W 14 x 426 B 172C586 b W 14 x 426 B 182C159 b W 14 x 426 B 182C535 b W 14 x 142 B 182C150 b W 14 x 142 B 181C686 b

a. Material A - ASTM A572-68 Grade 42 Ty 4 KLD, stress relieved at 1,100°F furnace cooled.

NAPS UFSAR Material B - ASTM A36-69, stress relieved at 1,100°F, furnace cooled.

b. Same as steam generator lower support - Unit 1 data (see Table 2).

5A Att. 1-13

Table 4 REACTOR COOLANT PUMP SUPPORTS - UNIT 1 HEATS OF MATERIAL Elongation Percent Heat Yield Tensile Reduction Hardness a

Description Material Number Point Strength Percent In. in Area BHN Bend C Mn P S Si V N W 14 x 605 B 182C090 45,000 76,250 27.5 8 55.2 143 OK .22 1.07 .012 .024 .27 W 14 x 426 B 171C871 b Revision 5209/29/2016 W 14 x 426 B 171C866 b W 14 x 426 B 182C159 b W 14 x 426 B 182C174 b W 14 x 426 B 172C963 44,081 71,180 29.0 8 55.4 170 OK .24 1.14 .012 .027 .06 W 14 x 176 B 182C156 39,766 64,775 30.5 8 59.1 137 OK .22 .65 .012 .020 .05 W 14 x 176 B 182C154 41,815 66,869 29.5 8 56.4 143 OK .23 .67 .010 .018 .07

a. Material B - ASTM A36-69, stress relieved at 1,100°F furnace cooled.
b. Same as steam generator lower support - Unit 1 data (see Table 2).

NAPS UFSAR 5A Att. 1-14

Table 5 REACTOR COOLANT PUMP SUPPORTS - UNIT 2 HEATS OF MATERIAL Elongation Percent Heat Yield Tensile Reduction in Hardness Description Materiala Number Point Strength Percent In. Area BHN Bend C Mn P S Si V N W 14 x 605 B 182C090 c W 14 x 426 B 171C871 b Revision 5209/29/2016 W 14 x 426 B 171C866 b W 14 x 426 B 182C159 b W 14 x 426 B 182C174 b W 14 x 426 B 172C963 c W 14 x 176 B 182C156 c W 14 x 176 B 182C154 c

a. Material B - ASTM A36-69, stress relieved at 1,100°F furnace cooled.
b. Same as steam generator lower support - Unit 1 data (see Table 2).
c. Same as reactor coolant pump support - Unit 1 data (see Table 4).

NAPS UFSAR 5A Att. 1-15

Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-16 Table 6 MATERIAL FROM BACK WELDMENT UNIT NO. 2 RCP SUPPORT STRUCTURE (CUBICLE C) MATERIAL MEETS ASTM A242 TYPE 1, 176 LB BEAM Mechanical Test Data Yield strength 58,000psi Tensile strength 76,100 psi Elong 32% in 2 in.

R.A. 70.6%

Charpy V-Notch Test Data (Long Rolling Direct-Flange Section 1 1/4 in. thick)

Specimen Temperature Number °F Ft/lbs MLE Percent Shear 1 80 24 25 15 2 80 25 26 15 3 100 35 34 28 4 100 36 36 28 5 120 36 35 35 6 120 38 36 35 7 140 92 72 58 8 140 113 88 71 9 160 92 76 62 10 160 97 77 69 11 180 80 65 58 12 180 120 87 81 Chemical Analysis Samplea Vand Nit. Cb C Chr. Ni Man Moly Cu Si P S A .01 .008 .01 .12 .59 .56 .87 .01 .29 .30 .11 .017 B .01 .008 .01 .12 .58 .56 .88 .01 .35 .31 .11 .015 C .01 -- -- .13 .58 .55 .88 >.02 .29 .34 .113 .020

a. Samples B and C removed from same beam (right beam looking in from back of structure).

Table 7 SPECIFIC DATA ON ORIGINAL FOUR HEATS CHARPY TESTEDa Reported heat Most probable heat designation designation as (based on Actual mill cert determined by Form of material location heat designation chemical analysis from which test Location from which removed from as traced from performed by specimen was test specimen structure or unit) structure piece number VEPCO removed was taken Revision 5209/29/2016 AB 182C535, 182C174, or 182C535 ASTM A36-69 test W 14 x 426 beam, Steam generator support 171C866 specimen taken from 3 in. flange in the unit 2, cubicle A, B, or C, longitudinal rolling direction corner middle level CD C9017, or A8225 A8225 ASTM A36-69 3 in. plate; specimen RC pump support unit 2, taken from longitudinal rolling cubicle A, B, or C, bracket direction piece F2A 182C535, 182C174, or 182C535 ASTM A36-69 W 14 x 426 beam; Steam generator support 171C866 specimen taken from 3 in. flange in unit 1, cubicle A, middle longitudinal rolling direction level, corner 2 W96 182C535, 182C174, or 182C174,b or ASTM A36-69 W 14 x 426 beam; Steam generator support 171C866 171C866 specimen taken from longitudinal unit 1, cubicle C, middle direction in beam web (2 in. thick) level, corner 3

a. Upon review of additional scrap material at the site, and evaluation of additional chemical analyses of the samples, it appears that what was originally designated as four heats is three heats (two heats from 426 lb A36 beams and one heat from a 3 in. thick A36 plate). It was also determined, however, that a total of only nine heats of 426 lb NAPS UFSAR beams were used in all structures.
b. These two chemistries are so close that analysis techniques are unable to differentiate between them. Chemistries that are very similar are the rule rather than the exception throughout the heats of 426 lb beams of A36 material used in these structures (see Table 2). Heat 182C535 can be differentiated by chemistry because it possesses a sulfur con-tent (0.031) approximately 50 percent higher than that of the other heats (average 0.020).

5A Att. 1-17

Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-18 Table 8 THROUGH THICKNESS CV PROPERTIES OF THE ORIGINAL FOUR SAMPLESa Specimen Designation and AB AB CD CD W96 W96 F2A F2A temperature of test 80°F 125°F 80°F 125°F 80°F 125°F 80°F 125°F Ft/lbs 12 25 10 26 8 20 12 25 16 27 13 30 11 35 14 26 23 32 14 30 18 39 15 30 Mills. 20 35 14 35 10 28 19 35 Lat. 24 38 17 36 15 44 20 35 Exp. 30 40 18 39 26 50 18 43

a. Notch in the longitudinal rolling direction.

Table 9 CHARPY V TESTS DATA FOR ADDITIONAL A-36 SAMPLES Specimen #1 Specimen #2 Specimen #3 VEPCO Test Mils Mils Mils.

Sample Mil. Cert Test Temp Lat Lat.  % Lat.  %

Number Heat # (4) Direction °F Ft-lbs Exp. % Shear Ft-lbs Exp. Shear Ft-lbs Exp. Shear Comment 1AM11F 182C174 L(2) 80 68 57 60 58 53 50 57 51 50 Revision 5209/29/2016 1AM11F or L 125 73 62 70 79 66 70 38 41 50 171C866 1AM11F TT(3) 80 10 13 10 14 17 10 17 18 10 1AM11F TT 125 25 28 30 26 28 30 27 33 40 1AM21F 182C174 L 80 61(61) 56(52) 50(50) 49(40) 47(39) 40(40) 19(22) 24(23) 30(30) (xx) =

Retest 1AM21F or L 125 73 65 70 82 73 70 72 62 70 171C866 1AM21F TT 80 20 21 20 13 15 10 11 13 10 1AM21F TT 125 18 27 40 20 25 30 17 23 30 1AM41F 182C174 L 80 48 46 40 36 37 30 36 36 30 1AM41F or L 125 101 81 90 64 59 60 81 59 70 1AM41F 171C866 TT 80 17 24 10 12 18 10 14 18 10 1AM41F TT 125 24 32 40 24 32 40 23 31 30 NAPS UFSAR 1BM11F 182C174 L 80 42 40 40 23 27 40 38 37 30 1BM11F 171C866, L 125 86 72 80 80 64 80 64 58 70 1BM11F or TT 80 16 20 10 14 17 10 15 18 10 1BM11F 182C535 TT 125 21 27 10 24 29 10 24 29 10 1BM21F 182C174 L 80 71 58 80 74 62 80 31 29 20 1BM21F or L 125 82 70 80 85 67 70 81 63 70 1BM21F 171C866 TT 80 16 17 10 14 18 10 13 17 10 5A Att. 1-19

Table 9 (continued)

CHARPY V TESTS DATA FOR ADDITIONAL A-36 SAMPLES Specimen #1 Specimen #2 Specimen #3 VEPCO Test Mils Mils Mils.

Sample Mil. Cert Test Temp Lat Lat.  % Lat.  %

Number Heat # (4) Direction °F Ft-lbs Exp. % Shear Ft-lbs Exp. Shear Ft-lbs Exp. Shear Comment 1BM21F TT 125 21 27 10 30 35 10 35 36 10 Revision 5209/29/2016 1BM21W 182C174 L 80 32 34 30 31 32 30 33 33 30 1BM21W or L 125 54 53 70 52 55 70 71 68 90 1BM21W 171C866 TT 80 12 14 10 12 16 10 8 11 10 1BM21W TT 125 24 27 30 15 20 30 19 25 30 1BM31F 182C535 L 80 68 63 60 72 61 60 55 52 50 1BM31F L 125 80 70 80 102 76 90 89 74 80 1BM31F TT 80 17 21 10 20 23 10 15 18 10 1BM31F TT 125 22 31 40 22 28 40 22 30 40 1BM41F L 80 47 42 30 58 52 40 53 48 40 1BM41F 182C174 L(2) 125 48(91) 46(70) 40(80) 32(55) 35(50) 30(60) 104(87) 78(69) 90(80) (xx) =

Retest 1BM41F or TT(3) 80 20 23 10 22 23 10 20 22 10 1BM41F 171C866 TT 125 22 26 30 25 28 30 20 22 20 1CM21F 182C535 L 80 63 59 40 64 56 60 80 71 70 NAPS UFSAR 1CM21F L 125 92 73 90 38 75 100 94 73 90 1CM21F TT 80 14 23 20 20 22 40 15 26 30 1CM21F TT 125 28 34 50 32 38 70 36 44 90 1CM22F 182C174 L 80 68 61 60 81 66 70 51 47 40 1CM22F or L 125 82 67 80 83 67 80 47 50 50 1CM22F TT 80 15 18 30 15 18 30 9 11 10 1CM22F TT 125 24 29 30 26 30 50 26 30 50 5A Att. 1-20

Table 9 (continued)

CHARPY V TESTS DATA FOR ADDITIONAL A-36 SAMPLES Specimen #1 Specimen #2 Specimen #3 VEPCO Test Mils Mils Mils.

Sample Mil. Cert Test Temp Lat Lat.  % Lat.  %

Number Heat # (4) Direction °F Ft-lbs Exp. % Shear Ft-lbs Exp. Shear Ft-lbs Exp. Shear Comment 1CM32F 182C174 TT 80 22 26 30 18 22 30 20 25 30 No longitud-Revision 5209/29/2016 inal test samples taken or TT 125 27 28 50 27 29 50 33 39 50 171C866 Notes:

(1) All samples removed from ASTM A-36-69 W14 x 426 beams, 3 thick Flange except 1BM21W which was removed from a web 2" thick.

(2) L = Longitudinal rolling direction.

(3) TT = Through thickness direction (also called short transverse direction notch always in long transverse direct.

(4) VEPCO chemical analysis - most probable heat direction.

NAPS UFSAR 5A Att. 1-21

Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-22 Table 10 STRESSES IN STEAM GENERATOR LOWER SUPPORTS, LOWER SUPPORT MEMBER FAILURE LOCA Member Stress Due to Stress Due to Break Number b, e Dead weight DBE Number Stress Total Stress 15 3.9 5.9 7 10.4 20.2 a 18 c - - 7 - -

20 c - - 7 - -

21 4.9 9.6 7 15.2 29.7 22 2.1 5.9 7 6.5 14.5 a 23 4.2 9.0 7 14.3 27.5 24 3.9 5.1 7 10.3 19.3 a 26 2.9 7.8 7 7.8 18.5 d 33 3.8 5.6 7 11.2 20.6 35 3.2 4.5 7 9.7 17.4 d 42 5.3 10.2 7 14.5 30.0 d 43 1.7 4.0 7 5.1 17.4 a 44 c - - 7 - -

45 c - - 7 - -

46 2.8 4.1 7 8.5 15.4 a 47 3.7 5.4 7 11.0 20.1 a 49 5.5 10.8 7 13.1 29.4 55 3.3 10.6 7 10.2 24.0 57 2.0 11.7 7 6.0 19.7 58 5.4 7.9 7 14.6 27.9 a 59 4.6 9.0 7 12.1 25.7 60 2.1 3.7 7 5.6 11.4 e 64 5.1 6.7 7 13.7 25.5 a

a. Component and total stresses adjusted to reflect stress at actual member end. All other component/total stresses not so noted conservatively reflect stresses at the nodes.
b. The members shown were chosen for inclusion in this table on the basis of satisfying one of the following conditions:

(LOCA 20.0 ksi or Seismic 9.0 ksi or Dead weight 3.4 ksi). Since these supports consist of in excess of 150 individual members, computer stress tabulation of all members for all cases was not maintained. Rather, a procedure was used to isolate members whose nominal stress values exceed defined screening limits for each load type. Members below this screening limit met the design allowables with conservative margin and were not tabulated in order to reduce the size of the data base requiring more vigorous evaluation. The above arbitrary values do not represent individual stress limits, but are only used to screen-out members that do not require further evaluation. The sum of stresses for such screened-out members is less than the sum of these three values (32.4 ksi) and thus satisfy the design limit of 0.9Y yield.

c. Member removed to demonstrate redundancy.
d. Member derived from integral model even though individual component stresses are less than footnote b criteria.
e. The support members given in this table are shown in Figures 1 and 2.

Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-23 Table 10 (continued)

STRESSES IN STEAM GENERATOR LOWER SUPPORTS, LOWER SUPPORT MEMBER FAILURE LOCA Member Stress Due to Stress Due to Break Number b, e Dead weight DBE Number Stress Total Stress 67 4.3 6.8 7 11.5 22.6 75 6.0 8.2 7 16.8 31.0 79 5.4 9.6 7 14.0 29.0 80 2.6 12.5 7 7.9 23.0 83 6.2 9.5 7 16.5 32.2 a 88 c - - 7 - -

89 3.3 8.7 7 9.2 21.2 e 93 3.3 15.0 7 9.9 28.2 a 98 5.2 8.3 7 13.8 27.3 210 9.2 4.1 7 8.4 20.7 a 211 5.0 8.2 7 13.7 26.9 a 212 c - - 7 - -

213 4.0 5.8 7 11.9 21.7 a 28 4.3 6.4 7 11.8 22.6 31 3.6 6.3 7 10.7 20.6 66 4.1 6.8 7 10.9 21.8 68 3.5 6.3 7 9.3 19.1 78 4.0 7.6 7 11.1 22.7

a. Component and total stresses adjusted to reflect stress at actual member end. All other component/total stresses not so noted conservatively reflect stresses at the nodes.
b. The members shown were chosen for inclusion in this table on the basis of satisfying one of the following conditions:

(LOCA 20.0 ksi or Seismic 9.0 ksi or Dead weight 3.4 ksi). Since these supports consist of in excess of 150 individual members, computer stress tabulation of all members for all cases was not maintained. Rather, a procedure was used to isolate members whose nominal stress values exceed defined screening limits for each load type. Members below this screening limit met the design allowables with conservative margin and were not tabulated in order to reduce the size of the data base requiring more vigorous evaluation. The above arbitrary values do not represent individual stress limits, but are only used to screen-out members that do not require further evaluation. The sum of stresses for such screened-out members is less than the sum of these three values (32.4 ksi) and thus satisfy the design limit of 0.9Y yield.

c. Member removed to demonstrate redundancy.
d. Member derived from integral model even though individual component stresses are less than footnote b criteria.
e. The support members given in this table are shown in Figures 1 and 2.

Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-24 Table 11 STRESSES IN STEAM GENERATOR LOWER AND REACTOR COOLANT PUMP SUPPORTS Stress Due LOCA Member to Dead Stress Due to Break Number c weight DBE Number a Stress Total Stress 210 3.2 b 6.4 7 23.8 d 30.2 211 7.8 b 13.4 7 16.5 d 29.9 212 3.7 b 5.6 f 7 11.5 e 20.8 213 5.1 g 10.3 f 7 15.7 e 31.1 133 0.1 g 13.0 f 2 20.6 e 33.7 148 0.1 g 2.3 f 12 20.7 e 23.1 149 0.1 9.8 2 14.3 24.2 155 0.3 9.4 12 17.0 26.7 156 0.3 9.3 12 18.2 27.8 157 0.1 9.5 2 22.6 32.3 158 0.2 9.5 2 21.1 20.9 159 0.1 12.5 2 14.4 27.0 160 0.1 g 9.9 f 2 17.7 e 27.7 161 0.0 11.4 12 19.8 31.2 162 0.0 11.8 12 17.7 29.5 163 0.1 g 9.0 f 2 14.5 e 23.6 164 0.0 g 7.1 f 2 17.3 e 24.4 165 0.0 g 7.3 f 12 15.8 e 23.1 166 0.0 g 6.5 f 12 8.6 e 25.1 169 0.0 7.0 f 12 22.7 e 29.7 Break Number Description 1 RPV outlet nozzle guillotine 2 RPV inlet nozzle guillotine (The effect of RPV movement is included.)

3 Steam generator inlet nozzle guillotine 4 Steam generator outlet nozzle guillotine 5 Reactor coolant pump suction nozzle guillotine 7 50 degree elbow at the entrados split 12 Loop closure weld guillotine

a. Description of pipe ruptures:
b. Separate deadweight stress listed for reference only.
c. Value listed includes stresses due to LOCA, RPV movement, and dead weight at actual member-end locations.

The support members given in this table a are shown in Figures 1 and 2.

d. Value listed includes stresses due to LOCA and dead weight at actual member-end locations. Corresponding seis-mic stress is unadjusted for conservatism.
e. Stress value listed due to LOCA at actual member-end locations.
f. Stress value due to DBE seismic event at actual member-end locations.
g. Stress value due to dead weight at actual member-end locations.

Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-25 Table 11 (continued)

STRESSES IN STEAM GENERATOR LOWER AND REACTOR COOLANT PUMP SUPPORTS Stress Due LOCA Member to Dead Stress Due to Break Number c weight DBE Number a Stress Total Stress 205 0.1 10.0 2 17.1 27.2 35 2.5 3.6 7 7.3 13.4 42 5.4 b 6.9 f 12 8.2 e 15.1 43 3.5 12.0 5 11.4 26.9 44 4.1 6. 7 12.7 22.9 45 5.3 b 5.8 f 7 20.8 d 26.6 46 5.5 8.7 f 7 16.4 e 30.6 47 5.6 b 8.7 f 7 20.6 d 29.3 49 4.9 8.6 f 12 16.8 e 25.4 55 2.5 10.2 4 8.1 20.8 57 1.8 11.5 12 7.0 20.3 58 5.2 b 7.7 7 17.5 25.2 59 3.6 7.8 7 8.8 20.2 60 4.5 6.5 7 13.4 24.4 64 5.1 6.9 7 16.5 28.5 67 4.7 7.4 7 13.9 26.0 75 4.9 6.9 7 13.3 25.1 79 4.3 8.5 4 10.5 23.3 80 2.0 12.2 12 9.5 23.7 83 5.6 b 9.0 7 19.1 d 28.1 Break Number Description 1 RPV outlet nozzle guillotine 2 RPV inlet nozzle guillotine (The effect of RPV movement is included.)

3 Steam generator inlet nozzle guillotine 4 Steam generator outlet nozzle guillotine 5 Reactor coolant pump suction nozzle guillotine 7 50 degree elbow at the entrados split 12 Loop closure weld guillotine

a. Description of pipe ruptures:
b. Separate deadweight stress listed for reference only.
c. Value listed includes stresses due to LOCA, RPV movement, and dead weight at actual member-end locations.

The support members given in this table a are shown in Figures 1 and 2.

d. Value listed includes stresses due to LOCA and dead weight at actual member-end locations. Corresponding seis-mic stress is unadjusted for conservatism.
e. Stress value listed due to LOCA at actual member-end locations.
f. Stress value due to DBE seismic event at actual member-end locations.
g. Stress value due to dead weight at actual member-end locations.

Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-26 Table 11 (continued)

STRESSES IN STEAM GENERATOR LOWER AND REACTOR COOLANT PUMP SUPPORTS Stress Due LOCA Member to Dead Stress Due to Break Number c weight DBE Number a Stress Total Stress 88 4.8 7.5 7 14.5 26.8 93 4.4 7.3 7 12.7 24.4 98 4.2 7.3 4 13.8 23.4 48 6.2 b 9.5 f 7 11.9 d 21.4 2 1.7 b 3.7 1 15.0 d 18.7 3 1.6 4.2 1 24.1 29.9 15 3.1 4.2 5 15.2 22.5 18 1.6 g 2.4 f 7 5.1 e 9.1 20 4.2 b 5.8 f 7 25.5 d 31.1 21 3.6 8.6 1 13.7 d 22.3 22 4.6 b 11.8 1 14.5 d 26.3 23 3.6 b 6.2 f 4 14.7 d 20.9 24 3.0 b 9.8 4 8.3 d 18.1 26 3.5 8.6 1 12.9 25.0 33 3.5 5.1 7 10.6 19.2 Break Number Description 1 RPV outlet nozzle guillotine 2 RPV inlet nozzle guillotine (The effect of RPV movement is included.)

3 Steam generator inlet nozzle guillotine 4 Steam generator outlet nozzle guillotine 5 Reactor coolant pump suction nozzle guillotine 7 50 degree elbow at the entrados split 12 Loop closure weld guillotine

a. Description of pipe ruptures:
b. Separate deadweight stress listed for reference only.
c. Value listed includes stresses due to LOCA, RPV movement, and dead weight at actual member-end locations.

The support members given in this table a are shown in Figures 1 and 2.

d. Value listed includes stresses due to LOCA and dead weight at actual member-end locations. Corresponding seis-mic stress is unadjusted for conservatism.
e. Stress value listed due to LOCA at actual member-end locations.
f. Stress value due to DBE seismic event at actual member-end locations.
g. Stress value due to dead weight at actual member-end locations.

Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-27 Figure 1 IDENTIFICATION OF R.C. PUMP SUPPORT MEMBERS

Figure 2 IDENTIFICATION OF STEAM GENERATOR MEMBERS Revision 5209/29/2016 NAPS UFSAR 5A Att. 1-28

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