ML14363A458
Text
B/B-UFSAR 11.0-i REVISION 9 - DECEMBER 2002 CHAPTER 11.0 -
RADIOACTIVE WASTE MANAGEMENT TABLE OF CONTENTS PAGE 11.0 RADIOACTIVE WASTE MANAGEMENT 11.1-1 11.1 SOURCE TERMS 11.1-1 11.1.1 Definition of Radioactive Source Terms 11.1-1 11.1.1.1 Design-Basis Shi elding Source Terms 11.1-1 11.1.1.2 Realistic Source Terms 11.1-1 11.1.1.3 Accident Sources 11.1-1 11.1.2 Basis for Radioactive Source Terms 11.1-2 11.1.2.1 Conservative Mod el for React or Coolant Activity 11.1-2 11.1.2.2 Realistic Model for Reactor Coolant Activity 11.1-3 11.1.3 Source Terms for Shielding Design Basis 11.1-4 11.1.4 Source Terms for Component Failure 11.1-5 11.1.5 Source Terms for Radwaste System Components 11.1-5 11.1.6 Sources of I n-Plant Airborne R adioactivity 11.1-5 11.1.7 Sources of Radio active Releases to the Environment 11.1-6 11.1.7.1 Gaseous Releases 11.1-6 11.1.7.2 Liquid Releases 11.1-6 11.1.8 Impact of Uprate on No rmal Operation Radiation Source Terms 11.1.9 References 11.1-6 11.2 LIQUID WASTE MANAGEMENT SYSTEMS 11.2-1 11.2.1 Design Bases 11.2-1 11.2.1.1 Safety Design Basis 11.2-1 11.2.1.2 Power Generation Design Basis 11.2-1 11.2.1.3 Expected Radioactive Releases 11.2-2 11.2.1.4 10 CFR 50 Comparison 11.2-2 11.2.1.5 10 CFR 20 Comparison 11.2-2a 11.2.1.6 Component Specifications 11.2-2a 11.2.1.7 Seismic Design and Quality Group 11.2-3 11.2.1.8 Facility and Equipment Design 11.2-3 11.2.1.8.1 Maintenance Operations 11.2-3 11.2.1.8.2 Floor, Wall, and Ceiling Coatings 11.2-3 11.2.1.9 Tank Level Control 11.2-3 11.2.1.10 Prevention of Un controlled Releases 11.2-4 11.2.1.11 ETSB-BTP 11-1 Comparison 11.1-5 11.2.2 System D escription 11.2-5 11.2.2.1 Steam Generator Blowdown Subsystem 11.2-6 11.2.2.1.1 Normal Operation 11.2-7 11.2.2.1.2 Circulating Water to Sec ondary System Leakage 11.2-8 11.2.2.1.3 Primary-to-Secon dary Leakage Concurrent with Failed Fuel 11.2-8
B/B-UFSAR 11.0-ii REVISION 7 - DECEMBER 1998 TABLE OF CONTENTS (Cont'd)
PAGE 11.2.2.1.4 Primary-to-Sec ondary Leakage Not Concurrent with Failed Fuel 11.2-8 11.2.2.1.5 Transient Operating Conditions 11.2-9 11.2.2.2 Nonblowdown Liquid Radwaste Subsystem 11.2-9 11.2.2.2.1 Auxiliary Building Equipment Drain 11.2-10 11.2.2.2.2 Auxiliary Building Floor Drain 11.2-11 11.2.2.2.3 Chemical Waste Drain 11.2-11
11.2.2.2.4 Regeneration Waste Drain 11.2-12 11.2.2.2.5 Laundry Drain 11.2-12 11.2.2.2.6 Turbine Building Equipment Drain 11.2-12 11.2.2.2.7 Turbine Building Floor Drain 11.2-13 11.2.2.2.8 Turbine Building Fire and Oil Sump 11.2-13 11.2.2.2.9 Condensate Polisher Sump 11.2-13 11.2.2.2.10 Waste Treatment System 11.2-13 11.2.2.3 Operating Procedures 11.2-14 11.2.2.4 Performance Tests 11.2-14 11.2.2.5 Control and Instrumentation 11.2-14 11.2.3 Radioactive Releases (Byron) 11.2-15 11.2.3.1 Release Points (Byron) 11.2-15 11.2.3.2 Dilution Factors (Byron) 11.2-15 11.2.3.3 Estimated Annual Average Doses (Byron) 11.2-15 11.2.3 Radioactive Releases (Braidwood) 11.2-16 11.2.3.1 Release Points (Braidwood) 11.2-16 11.2.3.2 Dilution Factors (Braidwood) 11.2-16 11.2.3.3 Estimated Annual Average Doses (Braidwood) 11.2-16 11.2.4 References 11.2-17 11.3 GASEOUS WASTE MANAGEMENT SYSTEMS 11.3-1 11.3.1 Design Bases 11.3-1 11.3.2 System D escription 11.3-2 11.3.2.1 System Design 11.3-2 11.3.2.2 Component Design 11.3-4 11.3.2.3 Instrumentation Design 11.3-4 11.3.2.4 Operating Procedure 11.3-5 11.3.2.5 Operations 11.3-5 11.3.2.6 Refueling 11.3-7 11.3.2.7 Auxiliary Services 11.3-7 11.3.2.8 Performance Tests 11.3-7 11.3.3 Radioactive Releases 11.3-8 11.3.3.1 NRC Requirements 11.3-8 11.3.3.2 Westinghouse PWR Experience Releases 11.3-8 11.3.3.3 Expected Gaseo us Waste Processing System Releases 11.3-8
B/B-UFSAR 11.0-ii (Cont'd)
REVISION 2 - DECEMBER 1990 TABLE OF CONTENTS (Cont'd)
PAGE 11.3.3.4 Estimated Total Releases 11.3-9 11.3.3.5 Effluent Concentrations and Dilution Factors 11.3-9 11.3.3.6 Release Points of Dilution Factors 11.3-9 11.3.3.7 Estimated Doses from Gaseous Releases 11.3-10 11.3.4 References 11.3-10
B/B-UFSAR 11.0-iii REVISION 12 - DECEMBER 2008 TABLE OF CONTENTS (Cont'd)
PAGE 11.4 SOLID WASTE MA NAGEMENT SYSTEM 11.4-1 11.4.1 Design Bases 11.4-1 11.4.1.1 Power Generation Design Bases 11.4-1 11.4.1.2 Safety Design Bases 11.4-1 11.4.1.3 Type of Waste 11.4-2 11.4.1.4 Expected Volumes and Isotopic Compositions 11.4-3 11.4.1.5 ETSB-BTP 11-3 Comparison 11.4-3 11.4.1.6 Comparison of Processing Capacity and Design Basis Waste Volumes (Byron) 11.4-4 11.4.1.6 Comparison of Proces sing Capacity and Design Basis Waste Volumes (Braidwood) 11.4-5 11.4.1.7 Solid Radwaste System Monitoring 11.4-7 11.4.2 System D escription 11.4-7 11.4.2.1 Deleted 11.4-7 11.4.2.2 Deleted 11.4-7 11.4.2.3 Deleted 11.4-7 11.4.2.4 Drum Handling Equipment 11.4-11 11.4.2.5 Smear Test and Label Station 11.4-12 11.4.2.6 Dry Waste Compactor (Byron) 11.4-12 11.4.2.7 Storage Areas 11.4-12 11.4.2.8 Control Room 11.4-13 11.4.2.9 Deleted 11.4-13 11.4.2.10 Deleted 11.4-13 11.4.2.11 Deleted 11.4-13 11.4.2.12 System Interfaces 11.4-13 11.4.2.13 Deleted 11.4-13 11.4.3 Volume Reduction System Description 11.4-14 11.4.4 Polymer/VR Product Drumming Station 11.4-14
B/B-UFSAR 11.0-iv REVISION 4 - DECEMBER 1992 TABLE OF CONTENTS (Cont'd)
PAGE 11.5 PROCESS AND EFFL UENT RADIOLOGICAL MONITORING AND SAMPLING SYSTEMS 11.5-1 11.5.1 Design Bases 11.5-1 11.5.1.1 Design Objectives 11.5-1 11.5.1.2 Design Criteria 11.5-3 11.5.2 System D escription 11.5-5 11.5.2.1 Instrumentation 11.5-5 11.5.2.2 Airborne Process and Effluent Monitors 11.5-7 11.5.2.2.1 Auxiliary Bu ilding Vent Stack Effluent 11.5-7 11.5.2.2.2 Auxiliary Buil ding Plant Areas (for Auxiliary Building Vent Exhausts) 11.5-7 11.5.2.2.3 Pipe Tunnel (f or Auxiliary Building Vent Exhausts) 11.5-7 11.5.2.2.4 Fuel-Handling Building Exhaust 11.5-7 11.5.2.2.5 Containment Purge Effluent 11.5-8 11.5.2.2.6 Fuel-Handling Incident in the Fuel Handling Building 11.5-8 11.5.2.2.7 Fuel-Handlin g Accident in the Containment Building 11.5-8 11.5.2.2.8 Main Control Room Outside Air Intakes A and B 11.5-8 11.5.2.2.9 Main Control Room Turbine Building Air Intakes A and B 11.5-9 11.5.2.2.10 Containment Atmosphere Monitoring 11.5-9 11.5.2.2.11 Miscel laneous Tank Vent Exhaust 11.5-10 11.5.2.2.12 Radwaste Area Vent Exhaust 11.5-10 11.5.2.2.13 SJAE/Gland Steam Exhaust 11.5-10 11.5.2.2.14 Gas Decay Tank Effluent 11.5-10
B/B-UFSAR 11.0-v TABLE OF CONTENTS (Cont'd)
PAGE 11.5.2.2.15 VR Systems Areas and Cubicles Ventilation Exhaust 11.5-11 11.5.2.2.16 TSC Ventilation System 11.5-11 11.5.2.2.17 Miscel laneous Process Monitors 11.5-11 11.5.2.2.18 Auxiliary Bu ilding Vent Stack Wide Range Gas Monitor 11.5-11 11.5.2.3 Liquid Effluent Monitors 11.5-11 11.5.2.3.1 Liquid Radwaste Effluent Monitor 11.5-12 11.5.2.3.2 Component Cooling Water Monitors 11.5-12 11.5.2.3.3 Steam Generator Blowdown 11.5-12 11.5.2.3.4 Blowdown Filters 11.5-12 11.5.2.3.5 Gross Failed Fuel Monitor 11.5-12 11.5.2.3.6 Miscellaneous Process Liquid Monitors 11.5-13 11.5.2.3.7 Turbine Building Fire and Oil Sump 11.5-13 11.5.2.3.8 Condensate Cleanup Area Sumps Discharge 11.5-13 11.5.2.4 Sampling 11.5-13 11.5.2.4.1 Process Sampling 11.5-14 11.5.2.4.2 Effluent Sampling 11.5-14 11.5.2.4.3 Representative Sampling 11.5-14 11.5.2.4.4 Analytical Procedures 11.5-14 11.5.2.5 Instrument Ins pection, Calibration, and Maintenance 11.5-15 11.5.2.5.1 Calibration 11.5-16 11.5.3 Effluent Monitoring and Sampling 11.5-16 11.5.4 Process Monitori ng and Sampling 11.5-16
B/B-UFSAR 11.0-vi REVISION 9 - DECEMBER 2002 CHAPTER 11.0 -
RADIOACTIVE WASTE MANAGEMENT LIST OF TABLES NUMBER TITLE PAGE 11.1-1 Parameters Used in the Calculation of Design Basis Primary Coolant Activities - Original and Uprated (***) 11.1-7 11.1-2 Design-Basis Rea ctor Coolant Fission and Corrosion Product Activity (Original Design) 11.1-10 11.1-3 Parameters Used in the Calculation of Realistic, Opera tional Basis Primary Coolant Activities 11.1-11 11.1-4 Realistic, Ope rational Basis Reactor Coolant Fission and Corrosion Product Activities 11.1-13 11.1-5 Maximum Realisti c, Operational Basis Waste Gas Decay Tank Activity for Gas Decay Tank Rupture 11.1-15 11.1-6 Realistic Sour ce Terms for Steam Generator Blowdo wn and Radioactive Drain Streams 11.1-16 11.1-7 Realistic Source Terms for Balance of Plant 11.1-20 11.1-8 Realistic Sour ce Terms for Radwaste System Filters and Demineralizers 11.1-24 11.1-9 Realistic Source Ter ms for NSSS Filters 11.1-28 11.1-10 Realistic So urce Terms for NSSS Demineralizers 11.1-31 11.1-11 Realistic Source Terms for C oncentrates and Spent Resin Tanks (Byron) 11.1-33 11.1-11 Realistic Sour ce Terms for High and Low Activity Spent Resin Tanks (Braidwood) 11.1-35 11.1-12 Deleted 11.1-13 Uprated Design-Basis Reactor Coolant Fission And Corrosion Pr oduct Activity 11.2-1 Expected Annual Average Releases of Radionuclides in Liquid Effluents 11.2-18 11.2-2 Parameters U sed in the GALE-PWR Computer Program (Original & Uprated) - Note 1 11.2-19 11.2-3 Pathways Doses f rom Liquid Effluents (Byron) 11.2-22 11.2-3 Pathways Doses f rom Liquid Effluents (Braidwood) 11.2-23 11.2-4 Comparison of Expected Liqui d Effluent Concentrations to 10 CFR 20 Limits (Byron) 11.2-24 11.2-4 Comparison of Expected Liqui d Effluent Concentrations to 10 CFR 20 Limits (Braidwood) 11.2-25 11.2-5 Liquid Radwaste System Components and Design Parameters Per Station 11.2-26 11.2-6 Design-Basis A nnual Average and Maximum Waste Stream Flows (Two Units) 11.2-32
B/B-UFSAR 11.0-vii REVISION 6 - DECEMBER 1996 LIST OF TABL ES (Cont'd)
NUMBER TITLE PAGE 11.2-7 Design-Basis P rocess Decontamination Factors 11.2-33 11.2-8 Consumption Fa ctors for the Maximum Exposed Individual 11.2-35 11.2-9 Summary of T ank Level Indicati on, Annunciators, and Overflows for Tanks Outside of Containment Poten tially Containing Radioactive Liquids 11.2-36 11.3-1 Gaseous Wast e Processing System Component Data 11.3-11 11.3-2 Gaseous Wast e Processing System Instrumentation Design Parameters 11.3-12 11.3-3 Process Paramete rs and Realistic, Operation Basis Activities in Gaseous Waste System 11.3-15 11.3-4 Assumptions Used in Calculating Expected System Activities 11.3-23 11.3-5 Typical Gase ous Releases From Operating Reactors 11.3-25 11.3-6 Expected Annual Average Release of Airborne Radionuclides 11.3-26 11.3-7 Comparison of Maximum Offsite Airborne Concentrations with 10 CFR 20 Limits (Byron) 11.3-30 11.3-8 Atmospheric Dilution Factors Used in Determining Offsite Doses (Byron) 11.3-31 11.3-9 Byron - Expected Individual Doses from Gaseous Effluents 11.3-32 11.3-7 Comparison of Maximum Offsite Airborne Concentrations with 10 CFR 20 Limits (Braidwood) 11.3-33 11.3-8 Atmospheric Dilution Factors Used in Determining Offsite Doses (Braidwood) 11.3-34 11.3-9 Braidwood - Expected Individual Doses from Gaseous Effluents 11.3-35 11.3-10 Exhaust Stack Airflow Tabulation 11.3-38 11.4-1 Solid Waste Mana gement Syste m Equipment and Storage Design Capacities (Byron) 11.4-52 11.4-2 Expected and Design Basis Annual Volumes of (Units 1 and 2)
Solid Waste Management System Output (Byron) 11.4-56 11.4-3 Plant Interfac es with Solid Radwaste System (Byron) 11.4-57 11.4-1 Solid Waste Mana gement Syste m Equipment and Storage Design Capacities (Braidwood) 11.4-64
B/B-UFSAR 11.0-viii REVISION 6 - DECEMBER 1996 LIST OF TABL ES (Cont'd)
NUMBER TITLE PAGE 11.4-2 Expected and Des ign Basis Annual Volumes of (Units 1 and 2)
Solid Waste Management System Output (Braidwood) 11.4-68 11.4-3 Plant Interface with Solid Radwaste System (Braidwood) 11.4-69 11.5-1 Airborne Process and Effluent Monitors 11.5-17 11.5-2 Process Liquid Monitors 11.5-26 11.5-3 Radiological Analysis Summary of Liquid Process Samples 11.5-30 11.5-4 Radiological Analysis Summary of Gaseous Process Samples 11.5-31 11.5-5 Radiological Analysis Summary of Liquid Effluent Samples 11.5-32 11.5-6 Radiological Analysis Summary of Gaseous Effluent Samples 11.5-33
B/B-UFSAR 11.0-ix REVISION 9 - DECEMBER 2002 CHAPTER 11.0 -
RADIOACTIVE WASTE MANAGEMENT LIST OF FIGURES NUMBER TITLE 11.2-1 through 11.2-41 Deleted 11.3-1 Deleted 11.3-2 Gaseous Wast e Processing System Flow Diagram 11.4-1 Radwaste Disposal Sy stem Flow Diagram (Byron) 11.4-1 Radwaste Disposal Syst em Flow Diagram (Braidwood) 11.4-2 Deleted 11.4-3 Deleted 11.4-4 Deleted
B/B-UFSAR 11.0-x REVISION 9 - DECEMBER 2002 CHAPTER 11.0 -
RADIOACTIVE WASTE MANAGEMENT DRAWINGS CITED IN THIS CHAPTER*
- The listed drawings are included as "General Re ferences" only; i.e., refer to the drawings to obtain ad ditional detail or to obtain background info rmation. These drawin gs are not part of the UFSAR. They are controlled by the Control led Documents Program. DRAWING* SUBJECT M-9 General Arrangement Floor Pl an At EL. 383'-0" Units 1 and 2 M-12 General Arrangement Radwaste
/Service Building Units 1 & 2 M-24-1 to -20 General Arrangements , Radiation Shield ing Units 1 &
2 M-48-1 Diagram of Waste Disposal 30,000 Gallon Release Tank Units 1 & 2 M-48-2 Diagram of Waste Disposal Steam Generator Blowdown Units 1 & 2 M-48-3A, -3B Diagram of Waste Disposal Blowdown Mixed Bed Demineralizer Units 1 & 2 M-48-4A, -4B Diagram of Waste Disposal Blowdown Monitor Tanks Units 1 & 2 M-48-4C Diagram of Waste Dis posal Vacuum Pumps M-48-5A, -5B Diagram of Waste Disposal Steam Generator Blowdown Units 1 & 2 M-48-6A, -6B Diagram of Waste Disposal Auxiliary Building Floor Drains Units 1 & 2 M-48-7 Diagram of Waste Disposal (Liquid) Chemical &
Demineralizer Waste Regen.
Drains Units 1 & 2 M-48-8 Diagram of Waste Disposal Laundry Waste Drains Units 1 & 2 M-48-9 Diagram of Waste Disposal Radwaste Evaporator Units 1 & 2 M-48-10 Diagram of Waste Disposal Radwaste Evaporator "OA" Units 1 & 2 M-48-11, -12 Diagram of Waste Disposal Radwaste Evaporator "OB" Units 1 & 2 M-48-13 Diagram of Waste Disposal Radwaste Evaporator Units 1 & 2 M-48-14 Diagram of Waste Disposal Radwaste Evaporator "OC" Units 1 & 2
B/B-UFSAR 11.0-xi REVISION 9 - DECEMBER 2002 DRAWINGS CITED IN TH IS CHAPTER* (Cont'd)
DRAWING* SUBJECT M-48-15 Diagram of Waste Disposal Radwaste Monitor Tanks Units 1 & 2 M-48-16 Diagram of Waste Disposal Turbine Building Floor Drains Units 1 & 2 M-48-17 Diagram of Waste Disposal Auxiliary Building Equipment Drains Units 1 & 2 M-48-18 Diagram of Waste Disposal Resin Removal Units 1 & 2 M-48-19 Diagram of Miscellaneous Sum ps & Pumps Units 1 & 2 M-48-20A,
-20B Diagram of Waste Disposal Blowdown Mixed Bed Demineralizer Units 1 & 2 M-48-21A, -21B, -21C Diagram of Waste Disposal Radwaste Mixed Bed Demineralizer Units 1 & 2 M-48-22 Diagram of Waste Disposal Turbine Building Equipment Drains Units 1 & 2 M-48-23 Diagram of Radioactive W aste Reprocessing &
Disposal Units 1 & 2 M-48-24 Diagram of Turbine Build ing Waste Oil Collection System Units 1 & 2 M-48-25 Diagram of Auxiliary Bui lding Waste Oil Collection System Units 1 & 2 M-48-28 Diagram of Auxiliary Building Leak D etection Sumps Units 1 & 2 M-48-29 Diagram of Auxil iary Building Chromated Drain Collection System Units 1 & 2 M-48-30 Diagram of Miscellaneous Sump & Pumps Units 1 & 2 M-38-31 Blowdown Radwaste Mixed Bed Demineralizer Regeneration Skid Units 1 & 2 M-48-32 Diagram of Cement Filling Station Units 1 & 2 M-48-37 Diagram of Turbi ne Bldg Equipm ent/Floor Drain Coalescers Units 1 & 2 M-48-38 Diagram of Radwaste Evap orator Ammonia Stripper "A" Unit 1 & 2 M-48-39 Diagram of Radwaste Evap orator Ammonia Stripper "B" Unit 1 & 2 M-48-40 Diagram of Radwaste Evap orator Ammonia Stripper "C" Unit 1 & 2 M-48A Composite Diagram of L iquid Radwaste Treatment Processing Units 1 & 2
B/B-UFSAR 11.0-xii REVISION 9 - DECEMBER 2002 DRAWINGS CITED IN TH IS CHAPTER* (Cont'd)
DRAWING* SUBJECT M-64 Diagram of Chemical & Vo lume Control
& Boron Thermal Regenera tion Unit 1 M-64A Diagram of Chemical & Vo lume Control
& Boron Thermal Regenera tion Unit 1 M-69 Diagram of Radioacti ve Waste Gas Sys tem Units 1 & 2
B/B-UFSAR 11.3-11 TABLE 11.3-1 GASEOUS WASTE PROCESSING SYSTEM COMPONENT DATA
WASTE GAS COMPRESSORS
Number 2
Type Liquid seal rotary type
Design Flow rate, N 2 40 (at 140° F, 2 psig), cfm Design pressure, psig 150
Design temperature, °F 180 Normal operating pressure, psig Suction 0.5 - 2.0 Discharge 0 - 110 Normal operating temperature, °F 60 - 140 GAS DECAY TANKS
Number 6
Volume, each, ft 3 600 Design pressure, psig 150
Design temperature, °F 180 Normal operating pressure, psig 0 - 125 Normal operating temperature, °F 50 - 140 Material of construction Carbon steel
B/B-UFSAR
11.3-12
REVISION 11 - DECEMBER 2006 TABLE 11.3-2 GASEOUS WASTE PROCESSING SYSTEM INSTRUMENTATION DESIGN PARAMETERS
DESIGN DESIGN INSTRUMENT LOCATION OF PRESSURE TEMP. ALARM CONTROL LOCATION OF NUMBER PRIMARY SENSOR (psig)
(°F) RANGE SETPOINT SETPOINT READOUT TEMPERATURE INSTRUMENTATION TI-1029 Seal water, compressor No. 1 150 300 30-300°F NA NA At Waste Gas (Dial Thermometer) Compressor
TI-1034 Seal water, compressor No. 2 150 300 30-300°F NA NA At Waste Gas (Dial Thermometer) Compressor
PRESSURE INSTRUMENTATION PICA-1025 Vent header Hi, 2.5 psig 3.0 psig WPS panel 100 180 0 - 5 psig (BR) (BR) 2.0 psig (BY) 2.0 psig (BY)
Lo 2.0 psig (BR) 0.5 psig (BY)
PC-1028 (AB) Compressor No. 1 150 180 0 - 150 psig Hi, 100 psig Lo, 30 psig 100 psig WPS panel PC-1035 (AB) Compressor No. 2 150 180 0 - 150 psig Hi, 100 psig Lo, 30 psig 100 psig WPS panel PICA-1036 Waste gas decay tank No. 1 150 180 0 - 150 psig Hi, 95 psig 95 psig WPS panel (BR) 100 psig (BY)
_____________________
F - Flow R - Radiation P - Pressure I - Indication L - Level C - Control T - Temperature A - Alarm
B/B-UFSAR
11.3-13 REVI SION 10 - DECEMBER 2004 TABLE 11.3-2 (Cont'd)
DESIGN DESIGN INSTRUMENT LOCATION OF PRESSURE TEMP. ALARM CONTROL LOCATION OF NUMBER PRIMARY SENSOR (psig)
(°F) RANGE SETPOINT SETPOINT READOUT PICA-1037 Waste gas decay tank No. 2 150 180 0 - 150 psig Hi, 95 psig 95 psig WPS panel (BR)
PICA-1038 Waste gas decay tank No. 3 150 180 0 - 150 psig Hi, 95 psig 95 psig WPS panel (BR) 100 psig (BY)
PICA-1039 Waste gas decay tank No. 4 150 180 0 - 150 psig Hi, 95 psig 95 psig WPS panel (BR) 100 psig (BY)
PI-1047 Nitrogen header 150 180 0 - 25 psig NA NA Local
PICA-1052 Waste gas decay tank No. 5 150 180 0 - 150 psig Hi, 95 psig 95 psig WPS panel (BR) 100 psig (BY)
PICA-1053 Waste gas decay tank No. 6 150 180 0 - 150 psig Hi, 95 psig 95 psig WPS panel (BR) 100 psig (BY)
PIA-1065 Hydrogen header 150 180 50 - 150 psig Hi, 130 psig NA WPS panel Lo, 90 psig PIA-1066 Nitrogen header 150 180 50 - 150 psig Hi, 110 psig NA WPS panel Lo, 90 psig
B/B-UFSAR
11
.3-14 REVISION 13 - DECEMBER 2010 TABLE 11.3-2 (Cont'd)
DESIGN DESIGN INSTRUMENT LOCATION OF PRESSURE TEMP. ALARM CONTROL LOCATION OF NUMBER PRIMARY SENSOR (psig)
(°F) RANGE SETPOINT SETPOINT READOUT LEVEL INSTRUMENTATION LICA-1030 Waste gas compressor No. 1 150 180 0 - 28 in. Hi, 15 in. (BR) Inches: WPS panel 21 in. (BY) 15, 13 Lo, 1 in. 10, 7, 1 (BR) 21, 15 7, 4, 1 (BY)
LICA-1032 Waste gas compressor No. 2 150 180 0 - 28 in. Hi, 15 in. (BR) Inches: WPS panel 21 in. (BY) 15, 13 Lo, 1 in. 10, 7, 1 (BR) 21, 15 7, 4, 1 (BY)
RADIATION INSTRUMENTATION RICA-014 Plant vent See Section 11.5
GAS ANALYZER Located in separate cubicle in Aux. Bldg.
O/AIT-GW8003 (Byron)/
O/AT-GW8003 (Braidwood) Oxygen 300 212 0-19.99% 2% (Byron) none Local O/AR-GW8003 (Braidwood) Oxygen 300 212 0-5% 2% none Local O/AIT-GW004 Oxygen 300 212 0-5% 2% none Local O/AIT-GW8000 (Byron)/
O/AT-GW8000 (Braidwood) Hydrogen 25 130 0-100% - none Local O/AR-GW8000 (Braidwood) Hydrogen 25 130 0-100% - none Local
B/B-UFSAR
11.3-15
REVISION 3 - DECEMBER 1991 TABLE 11.3-3 PROCESS PARAMETERS AND REALISTIC, OPERATION BASIS ACTIVITIES IN GASEOUS WASTE SYSTEM(1) (CONCENTRATIONS IN
µC/cm 3)
POS NO.(2) LOCATION PRESSURE (psig) TEMP. (°F) FLOW RATE (cm 3/day) KR83M(4) KR85M(4) KR85 KR87 KR88 1 Unit 1 RCDT Vent 1.5 170 max. 1.14E+6 6.6E-04 1.9E-06 1.0E-04 1.0E-05 1.6E-05 2 Unit 2 RCDT Vent 1.5 170 max. 1.14E+6 6.6E-04 1.9E-06 1.0E-04 1.0E-05 1.6E-05 3 Sampling System VCT Vent Unit 1 1.5 115 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 4 Sampling System VCT Vent Unit 2 1.5 115 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 5 Vent Boron Recycle Holdup Tank - - 2.18E+7 1.2E-05 2.9E-08 9.5E-05 4.7E-07 3.2E-07 Vent 6 Gas Analyzer 3.5 VAR 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 7 Waste Disposal System SRST Vent - - 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 8 BRS Evaporator Unit 1 Vent (3) 1.5 155 3.82E+5 8.1E-04 1.9E-06 1.9E-02 3.2E-05 2.1E-05 9 BRS Evaporator Unit 2 Vent (3) 1.5 155 3.82E+5 8.1E-04 1.9E-06 1.9E-02 3.2E-05 2.1E-05 10 CVCS VCT Vent Unit 1 1.5 115 0 1.0E-01 8.8E-01 1.6E+01 2.2E-01 1.3E+00 11 CVCS VCT Vent Unit 2 1.5 115 0 1.0E-01 8.8E-01 1.6E+01 2.2E-01 1.3E+00 12 Combination of Normal Letdown 1.5 VAR 2.48E+7 4.5E-04 1.1E-06 7.8E-03 1.5E-05 1.2E-05 GWPS (5) 13 Compressor Recirculation Line 1.5 140 0 4.5E-04 1.1E-06 7.8E-03 1.5E-05 1.2E-05
B/B-UFSAR
11.3-16 REVISI ON 1 - DECEMBER 1989 TABLE 11.3-3 (Cont'd)
POS NO.(2) LOCATION PRESSURE (psig) TEMP. (°F) FLOW RATE (cm 3/day) KR89 XE131M(4) XE144M(4) XE133 XE135M(4) 14 Compressor Inlet 1.5 VAR 2.48E+7 4.5E-04 1.1E-06 7.8E-03 1.5E-05 1.2E-05 15 Compressor Inlet 0.5 VAR 2.48E+7 4.5E-04 1.1E-06 7.8E-03 1.5E-05 1.2E-05 16 Downstream of Compressor 110 max. 140 2.48E+7 4.5E-04 1.1E-06 7.8E-03 1.5E-05 1.2E-05 17 Compressor Outlet to Gas Decay - - 0 4.5E-04 1.1E-06 7.8E-03 1.5E-05 1.2E-05 Tanks 18 Inlet to Filling Gas Decay Tanks 110 max. 140 2.48E+7 4.5E-04 1.1E-06 7.8E-03 1.5E-05 1.2E-05 19 Line to Gas Decay Tank Header 110 AMB VAR 5.4E-06 3.0E-09 7.8E-03 1.2E-06 2.0E-07 20 Discharge Line 20 AMB VAR 0.0E+00 0.0E+00 7.7E-03 0.0E+00 0.0E+00 21 Discharge Line 1 AMB VAR 0.0E+00 0.0E+00 7.7E-03 0.0E+00 0.0E+00 22 Gas Analyzer 3.5 VAR 0 0.0E+00 0.0E+00 0.0E-00 0.0E+00 0.0E+00 23 From Gas Decay Tanks to Compressor 110 AMB 1.64E+8 5.4E-06 3.0E-09 7.8E-03 1.2E-06 2.0E-07 Inlet 24 From Gas Decay Tanks to BRS 3 AMB 1.64E+8 5.4E-06 3.0E-09 7.8E-03 1.2E-06 2.0E-07 HTs(6)
___________________
AMB - Ambient VAR - Variable
B/B-UFSAR 11.3-17 TABLE 11.3-3 (Cont'd)
POS NO.(2) LOCATION PRESSURE (psig) TEMP. (°F) FLOW RATE (cm 3/day) KR89 XE131M(4) XE133M(4) XE133 XE135M(4) 1 Unit 1 RCDT Vent 1.5 170 max. 1.14E+6 6.4E-06 2.1E-05 1.7E+00 3.1E+01 1.1E-01 2 Unit 2 RCDT Vent 1.5 170 max. 1.14E+6 6.4E-06 2.1E-05 1.7E+00 3.1E+01 1.1E-01 3 Sampling System VCT Vent Unit 1 1.5 115 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 4 Sampling System VCT Vent Unit 2 1.5 115 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 5 Vent Boron Recycle Holdup Tank - - 2.18E+7 9.4E-08 9.9E-06 2.5E-02 8.6E+00 1.6E-03 Vent 6 Gas Analyzer - - 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 7 Waste Disposal System SRST Vent - - 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 8 BRS Evaporator Unit 1 Vent (3) 1.5 155 3.82E+5 6.2E-06 1.1E-03 1.7E+00 7.3+02 1.1E-01 9 BRS Evaporator Unit 2 Vent (3) 1.5 155 3.82E+5 6.2E-06 1.1E-03 1.7E+00 7.3+02 1.1E-01 10 CVCS VCT Vent Unit 1 1.5 115 0 1.0E-03 1.6E+00 2.4E+00 2.2E+02 1.2E-02 11 CVCS VCT Vent Unit 2 1.5 115 0 1.0E-03 1.6E+00 2.4E+00 2.2E+02 1.2E-02 12 Combination of Normal Letdown 1.5 VAR 2.48E+7 3.7E-06 4.6E-04 9.9E-01 3.1E+02 6.4E-02 GWPS (5) 13 Compressor Recirculation Line 1.5 140 0 3.7E-06 4.6E-04 9.9E-01 3.1E+02 6.4E-02 14 Compressor Inlet 1.5 VAR 2.48E+7 3.7E-06 4.6E-04 9.9E-01 3.1E+02 6.4E-02
B/B-UFSAR
11.3-18 REVISI ON 1 - DECEMBER 1989 TABLE 11.3-3 (Cont'd)
POS NO.(2) LOCATION PRESSURE (psig) TEMP. (°F) FLOW RATE (cm 3/day) KR89 XE131M(4) XE133M(4) XE133 XE135M(4) 15 Compressor Inlet 0.5 VAR 2.48E+7 3.7E-06 4.6E-04 9.9E-01 3.1E+02 6.4E-02 16 Downstream of Compressor 110 max. 140 2.48E+7 3.7E-06 4.6E-04 9.9E-01 3.1E+02 6.4E-02 17 Compressor Outlet to Gas Decay - - 0 3.7E-06 4.6E-04 9.9E-01 3.1E+02 6.4E-02 Tank 18 Inlet to Filling Gas Decay 110 max. 140 2.48E+7 3.7E-06 4.6E-04 9.9E-01 3.1E+02 6.4E-02 Tanks 19 Line to Gas Decay Tank Header 110 AMB VAR 1.2E-09 3.5E-04 1.6E-03 1.8E-02 1.0E-04 20 Discharge Line 20 AMB VAR 0.0E+00 1.0E-05 0.0E+00 6.4E-02 0.0E+00 21 Discharge Line 1 AMB VAR 0.0E+00 1.0E-05 0.0E+00 6.4E-02 0.0E+00 22 Gas Analyzer 2 AMB 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 23 From Gas Decay Tank To 110 AMB 1.64E+8 1.2E-09 3.5E-04 1.6E-03 1.8E-02 1.0E-04 Compressor Inlet 24 From Gas Decay Tanks to BRS 3 AMB 1.64E+8 1.2E-09 3.5E-04 1.6E-03 1.8E-02 1.0E-04 Hts(6)
___________________ AMB - Ambient VAR - Variable
B/B-UFSAR 11.3-19 TABLE 11.3-3 (Cont'd)
POS NO.(2) LOCATION PRESSURE (psig) TEMP. (°F) FLOW RATE (cm 3/day) XE135 XE137 XE138 I130 I131 1 Unit 1 RCDT Vent 1.5 170 max. 1.14E+6 4.9E+01 1.4E-05 4.1E-01 1.1E-05 1.8E-06 2 Unit 1 RCDT Vent 1.5 170 max. 1.14E+6 4.9E+01 1.4E-05 4.1E-01 1.1E-05 1.8E-06 3 Sampling System VCT Vent Unit 1 1.5 115 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 4 Sampling System VCT Vent Unit 2 1.5 115 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 5 Boron Recycle Holdup Tank Vent - - 2.18E+7 1.8E+00 2.1E-07 6.2E-03 3.9E-08 5.7E-08 6 Gas Analyzer - - 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 7 Waste Disposal System SRST Vent - - 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 8 BRS Evaporator Unit 1 Vent (3) 1.5 1.5 3.82E+5 1.2E+02 1.4E-05 4.1E-01 0.0E+00 0.0E+00 9 BRS Evaporator Unit 2 Vent (3) 1.5 1.5 3.82E+5 1.2E+02 1.4E-05 4.1E-01 0.0E+00 0.0E+00 10 CVCS VCT Vent Unit 1 1.5 115 0 3.0E+00 2.2E-03 3.7E-02 0.0E+00 0.0E+00 11 CVCS VCT Vent Unit 2 1.5 115 0 3.0E+00 2.2E-03 3.7E-02 0.0E+00 0.0E+00 12 Combination of Normal Letdown to 1.5 VAR 2.48E+7 5.9E+01 8.1E-06 2.4E-01 2.0E-06 3.4E-07 GWPS (5) 13 Compressor Recirculation Line 1.5 140 0 5.9E+01 8.1E-06 2.4E-01 2.0E-06 3.4E-07 14 Compressor Inlet 1.5 VAR 2.48E+7 5.9E+01 8.1E-06 2.4E-01 2.0E-06 3.4E-07 15 Compressor Inlet 0.5 VAR 2.48E+7 5.9E+01 8.1E-06 2.4E-01 2.0E-06 3.4E-07
B/B-UFSAR
11.3-20
REVISION 1 - DECEMBER 1989 TABLE 11.3-3 (Cont'd)
POS NO.(2) LOCATION PRESSURE (psig) TEMP. (°F) FLOW RATE (cm 3/day) XE135 XE137 XE138 I130 I131 16 Downstream of Compressor 110 max. 140 2.48E+7 5.9E+01 8.1E-06 2.4E-01 2.0E-06 3.4E-07 17 Compressor Outlet to Gas Decay Tanks - - 0 5.9E+01 8.1E-06 2.4E-01 2.0E-06 3.4E-07 18 Inlet to Filling Gas Decay Tanks 110 max. 140 2.48E+7 5.9E+01 8.1E-06 2.4E-01 2.0E-06 3.4E-07 19 Line to Gas Decay Tank Header 110 AMB VAR 3.4E+00 3.3E-09 4.3E-04 1.5E-07 2.3E-07 20 Discharge Line 20 AMB VAR 0.0E+00 0.0E+00 0.0E+00 0.0E+00 1.3E-09 21 Discharge Line 1 AMB VAR 0.0E+00 0.0E+00 0.0E+00 0.0E+00 1.3E-09 22 Gas Analyzer 2 AMB 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 23 From Gas Decay Tanks To Compressor 110 AMB 1.64E+8 3.4E+00 3.3E-09 4.3E-04 1.5E-07 2.3E-07 Inlet 24 From Gas Decay Tanks To BRS HTs(6) 3 AMB 1.64E+8 3.4E+00 3.3E-09 4.3E-04 1.5E-07 2.3E-07
___________________
AMB - Ambient VAR - Variable
B/B-UFSAR 11.3-21 TABLE 11.3-3 (Cont'd)
POS NO.(2) LOCATION PRESSURE (psig) TEMP. (°F) FLOW RATE (cm 3/day) I132 I133 I134 I135 1 Unit 1 RCDT Vent 1.5 170 max. 1.14E+6 1.6E-07 2.3E-06 4.4E-08 8.4E-07 2 Unit 1 RCDT Vent 1.5 170 max. 1.14E+6 1.6E-07 2.3E-06 4.4E-08 8.4E-07 3 Sampling System VCT Vent Unit 1 1.5 115 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 4 Sampling System VCT Vent Unit 2 1.5 115 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 5 Boron Recycle Holdup Tank Vent - - 2.18E+7 2.9E-10 1.2E-08 7.4E-11 2.1E-09 6 Gas Analyzer - - 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 7 Waste Disposal System SRST Vent - - 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 8 BRS Evaporator Unit 1 Vent (3) 1.5 155 3.82E+5 0.0E+00 0.0E+00 0.0E+00 0.0E+00 9 BRS Evaporator Unit 2 Vent (3) 1.5 155 3.82E+5 0.0E+00 0.0E+00 0.0E+00 0.0E+00 10 CVCS VCT Vent Unit 1 1.5 155 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 11 CVCS VCT Vent Unit 2 1.5 155 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 12 Combination of Normal Letdown to GWPS (5) 1.5 VAR 2.48E+7 2.8E-08 4.1E-07 7.6E-09 1.5E-07 13 Compressor Recirculation Line 1.5 140 0 2.8E-08 4.1E-07 7.6E-09 1.5E-07 14 Compressor Inlet 1.5 VAR 2.48E+7 2.8E-08 4.1E-07 7.6E-09 1.5E-07 15 Compressor Inlet 0.5 VAR 2.48E+7 2.8E-08 4.1E-07 7.6E-09 1.5E-07
B/B-UFSAR
11.3-22 REVISI ON 1 - DECEMBER 1989 TABLE 11.3-3 (Cont'd)
POS NO.(2) LOCATION PRESSURE (psig) TEMP. (°F) FLOW RATE (cm 3/day) I132 I133 I134 I135 16 Downstream of Compressor 110 max. 140 2.48E+7 2.8E-08 4.1E-07 7.6E-09 1.5E-07 17 Compressor Outlet to Gas Decay Tanks - - 0 2.8E-08 4.1E-07 7.6E-09 1.5E-07 18 Inlet to Filling Gas Decay Tanks 110 max. 140 2.48E+7 2.8E-08 4.1E-07 7.6E-09 1.5E-07 19 Line to Gas Decay Tank Header 110 AMB VAR 3.9E-10 5.4E-08 4.1E-11 6.1E-09 20 Discharge Line 20 AMB VAR 0.0E+00 0.0E+00 0.0E+00 0.0E+00 21 Discharge Line 1 AMB VAR 0.0E+00 0.0E+00 0.0E+00 0.0E+00 22 Gas Analyzer 2 AMB 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 23 From Gas Decay Tanks To Compressor Inlet 110 AMB 1.64E+8 3.9E-10 5.4E-08 4.1-11 6.1E-09 24 From Gas Decay Tanks To BRS HTs (6) 3 AMB 1.64E+8 3.9E-10 5.4E-08 4.1-11 6.1E-09
___________________
AMB - Ambient VAR - Variable
B/B-UFSAR 11.3-23 TABLE 11.3-3 (Cont'd)
NOTES:
- 1. This is a synthe sis of information from operating reactors.
- 2. These position numbe rs correspond to positions marked on Figure 11.3-2.
- 3. Boron Recycle System (BRS).
- 4. Metastable (M).
- 5. Gaseous Waste Pr ocessing System (GWPS).
- 6. Holdup Tank (HT)
B/B-UFSAR
11.3-24 REVISION 3
- DECEMBER 1991 TABLE 11.3-4 ASSUMPTIONS USED IN CALC ULATING EXPECTED SYSTEM ACTIVITIES A. EXPECTED SYSTEM ACTIVITY
- 1. The major inputs to the gas sy stem during normal operation are vents on the Boron Recyc le System (BRS) holdup tanks (HUT), reactor coolant drain tanks (RCDT) and BRS evaporators. Inputs from the gas analyzer sampling system and CVCS volume control tank are assumed to be negligible.
- 2. Reactor coolant gase ous activities are b ased on Regulatory Guide 1.112 as modified to reflect Byr on/Braidwood plant parameters.
- 3. Twenty-five percent of dissolved radioga ses in the reactor coolant entering the RCDTs a nd HUTs leave solution and enter the vapor space.
- 4. Radioactive decay was assumed while the BRS HUTs, RCDTs and gas decay tanks were filling.
No additional decay was assumed in the evaporator.
- 5. The BRS HUT is assum ed to be filled to 80% capacity before processing by the BRS evaporat or. The RCDTs are assumed to be filled to 280 ga llons before draining.
- 6. Values for liquid flow rates to the ta nks were based on estimates of ann ual average flows:
BRS HUT flow 1.0 gpm (0.5 gpm per unit) RCDT flow 300 gpd (per each unit)
BRS Evaporator flow 1.0 gpm (0.5 gpm/evaporator - from BRS HUTs)
- 7. The plant capacity factor is 0.8.
- 8. The iodine parti tion coefficient in the RCDTs and BRS HUTs was: liquid in cc/Ci vapor in cc/Ci 10 X 5.7 3µµ (Based on Regulatory Guide 1.112).
- 9. The hydrogen con centration in the primary coolant was assumed 35 cc/kg.
B/B-UFSAR
11.3-2 5 REVISION 3 -
DECEMBER 1991 TABLE 11.3-4 (Cont'd)
B. ANNUAL RELEASES The following additional assumptions were us ed in calculating expected annual releases:
- 1. One refueling per ye ar per unit was assu med, with complete degassing of reactor coolant and also transfer of noble gases and iodines present in the volume control tank vapor space at shutdown to the gaseous waste s ystem. This gaseous activity is rele ased after 60 days decay for this analysis only.
- 2. Kr-85 release to the environment is based on an entry rate of 0.15 Ci/MWt-yr Kr
-85 into the primary coolant. It was assumed that all Kr-85 entering the cool ant is eventually released to the environment.
- 3. From the calcula tion of system activities, t he activity in a single gas decay tank was determined a fter 60 days decay. It was assumed that one tank was released every 60 days for purposes of this analysis only.
B/B-UFSAR 11.3-26 TABLE 11.3-5 TYPICAL GASEOUS RELEASES FROM OPERATING REACTORS
NOBLE GASES (10 3 Ci) 73 74 75 R. E. Ginna 0.576 0.78 1.81 Connecticut Yankee 0.032 0.008 1.81
San Onofre 11.0 1.78 1.07 Surry 1 & 2 0.87 54.4 9.47
H. B. Robinson 2 3.1 0.27 0.707
Point Beach 1 & 2 5.75 9.71 32.1
IODINES (Ci) 73 74 75 R. E. Ginna 0.0006 0.0004 0.0037 Connecticut Yankee 0.0013 0.0001 0.0009 San Onofre 0.42 0.0002 0.0046
Surry 1 & 2 0.042 0.071 0.0456 H. B. Robinson 2 0.296 0.012 0.0115 Point Beach 1 & 2 0.011 0.098 0.0188
B/B-UFSAR
11.3-27 R
EVISION 1 - DECEMBER 1989 TABLE 11.3-6 EXPECTED ANNUAL AVERAGE RELEASE OF AIRBORNE RADIONUCLIDES
- , ** GASEOUS RELEASE RATE - CURIES PER YEAR PRIMARY SECONDARY BLOWDOWN AIR COOLANT COOLANT GAS STRIPPING BUILDING VENTILATION VENT EJECTOR NUCLIDE (µCi/g) (µCi/g) SHUTDOWN CONTINUOUS REACTOR AUXILIARY TURBINE OFF-GAS EXHAUST TOTAL KR 83M 2.265-02 6.255-09 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 KR 85M 1.184-01 3.337-08 0.0 0.0 0.0 3.0+00 0.0 0.0 2.0+00 5.0+00
KR 85 1.051-01 2.944-08 5.1+01 5.7+02 7.4+01 2.0+00 0.0 0.0 1.0+00 7.0+02
KR 87 6.474-02 1.726-08 0.0 0.0 0.0 1.0+00 0.0 0.0 0.0 1.0+00
KR 88 2.156-01 5.928-08 0.0 0.0 0.0 5.0+00 0.0 0.0 3.0+00 8.0+00
KR 89 5.399-03 1.512-09 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
XE131M 1.035-01 2.917-08 4.0+00 1.5+01 1.7+01 2.0+00 0.0 0.0 1.0+00 3.9+01
XE133M 2.293-01 6.461-08 0.0 0.0 7.0+00 5.0+00 0.0 0.0 3.0+00 1.5+01
XE133 1.804+01 5.010-06 2.4+01 4.7+01 1.3+03 3.8+02 0.0 0.0 2.4+02 2.0+03 XE135M 1.404-02 3.887-09 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
XE135 3.755-01 1.041-07 0.0 0.0 2.0+00 8.0+00 0.0 0.0 5.0+00 1.5+01
- 0.0 appearing in the table indicates release is less than 1.0 Ci/yr for noble gas, 0.0001 Ci/yr for I.
- For one unit. KEY: 4.5-03 = 4.5 x 10
-3 B/B-UFSAR
11.3-28 R
EVISION 1 - DECEMBER 1989 TABLE 11.3-6 (Cont'd)
GASEOUS RELEASE RATE - CURIES PER YEAR PRIMARY SECONDARY BLOWDOWN AIR COOLANT COOLANT GAS STRIPPING BUILDING VENTILATION VENT EJECTOR NUCLIDE (µCi/g) (µCi/g) SHUTDOWN CONTINUOUS REACTOR AUXILIARY TURBINE OFF-GAS EXHAUST TOTAL XE137 9.719-03 2.700-09 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
XE138 4.751-02 1.296-08 0.0 0.0 0.0 1.0+00 0.0 0.0 0.0 1.0+00 TOTAL NOBLE GASES 2.8+03 I 131 2.795-01 4.215-05 0.0 0.0 1.7-03 4.4-02 2.3-03 0.0 2.8-03 5.1-02
I 133 3.986-01 3.831-05 0.0 0.0 7.7-04 6.3-02 2.1-03 0.0 4.0-03 7.0-02
TRITIUM GASEOUS RELEASE 1000 CURIES/YR
B/B-UFSAR 11.3-29 TABLE 11.3-6 (Cont'd)
AIRBORNE PARTICULATE RELEASE RATE - CURIES PER YEAR 1
WASTE GAS BUILDING VENTILATION NUCLIDE SYSTEM REACTOR AUXILIARY TOTAL MN 54 4.5-03 6.1-06 1.8-04 4.7-03 FE 59 1.5-03 2.1-06 6.0-05 1.6-03 CO 58 1.5-02 2.1-05 6.0-04 1.6-02 CO 60 7.0-03 9.5-06 2.7-04 7.3-03 SR 89 3.3-04 4.7-07 1.3-05 3.4-04 SR 90 6.0-05 8.4-08 2.4-06 6.2-05 CS134 4.5-03 6.1-06 1.8-04 4.7-03 CS137 7.5-03 1.1-05 3.0-04 7.8-03
- In addition to these re leases, 25 Ci/yr of argo n-41 are released from the containment and 8 Ci/yr of carbon-14 are released from the w aste gas processing sy stem. This table was developed taking into ac count both releases from normal oper ations and also operational occurrences.
KEY: 4.5-03 = 4.5 x 10
-3 B/B-UFSAR
11.3-3 0 REVISION 6 -
DECEMBER 1996 TABLE 11.3-6 (Cont'd)
VOLUME REDUCTION SYSTEM*
RELEASE RATE (Ci/yr)
Noble Gases: Xe 131m 5.1-01 Xe 133m 1.2+00 Xe 133 2.1+01
Halogens: I 131 2.8-03 I 132 3.7-03 I 133 2.1-03 Tritium: H 3 2.6+01
Particulates: Cr 51 5.3-08 Fe 55 7.0-07 Co 58 6.0-07 Co 60 9.2-08 Ni 63 7.0-07 Y 91 1.5-09 Mo 99 3.5-07 Tc 99m 2.1-09 Te 132 1.5-07 Cs 134 1.1-05 Cs 136 1.9-07 Cs 137 7.4-07
KEY: 5.1-01 = 5.1x10
-1
- The original est imate included r elease data for the volume reduction system. This system is no longer used.
BYRON-UFSAR 11.3-31 REVISION 5 - DECEMBER 1994 TABLE 11.3-7 COMPARISON OF MAXIMU M OFFSITE AIRBORNE CONCENTRATIONS WITH 10 CFR 20 LIMITS MAXIMUM SITE ANNUAL RELEASE BOUNDARY
- FROM ONE UNIT CONCENTRATION CONCENTRATION ISOTOPE (Ci/yr)
(µCi/ml) (µCi/ml) H 3 1.0+03 3.5-11 2.0-07 C 14 8.0+00 2.8-13 1.0-07 Ar 41 2.5+01 8.8-13 4.0-08 Kr 85m 5.0+00 1.8-13 1.0-07 Kr 85 7.0+02 2.5-11 3.0-07 Kr 87 1.0+00 3.5-14 2.0-08 Kr 88 8.0+00 2.8-13 2.0-08 Xe 131m 4.0+01 1.4-12 4.0-07 Xe 133m 1.6+01 5.6-13 3.0-07 Xe 133 2.0+03 7.0-11 3.0-07 Xe 135 1.5+01 5.3-13 1.0-07 Xe 138 1.0+00 3.5-14 3.0-08 I 131 5.4-02 1.9-15 1.0-10 I 132 3.7-03 1.3-16 3.0-09 I 133 7.2-02 2.5-15 4.0-10 Cr 51 5.3-08 1.9-21 8.0-08 Mn 54 4.7-03 1.7-16 1.0-09 Fe 55 7.0-07 2.5-20 3.0-08 Fe 59 1.6-03 5.6-17 2.0-09 Co 58 1.6-02 5.6-16 2.0-09 Co 60 7.3-03 2.6-16 3.0-10 Ni 63 7.0-07 2.5-20 2.0-09 Sr 89 3.4-04 1.2-17 3.0-10 Sr 90 6.2-05 2.2-18 3.0-11 Y 91 1.5-09 5.3-23 1.0-09 Mo 99 3.5-07 1.2-20 7.0-09 Tc 99m 2.1-09 7.4-23 5.0-07 Te 132 1.5-07 5.3-21 4.0-09 Cs 134 4.7-03 1.7-16 4.0-10 Cs 136 1.9-07 6.7-21 6.0-09 Cs 137 7.8-03 2.7-16 5.0-10
- 0.26 mi E /Q = 1.11 x 10
-6 sec/m 3 ** Limits used are those that were in effect at the time of the analysis.
KEY: 3.5 - 11 = 3.5 x 10-11 BYRON-UFSAR 11.3-32 REVISION 1 - DECEMBER 1989 TABLE 11.3-8 ATMOSPHERIC DILUTION FACTORS USED IN DETERMINING OFFSITE DOSES
/Q 2 D/Q* LOCATION (sec/m
- 3) (l/m 2) Nearest site boundary (0.26 mi E) 1.11 - 06 7.86 - 09
Nearest residence (0.30 mi ESE) 7.61 - 07 6.39 - 09 Nearest garden (0.60 mi SW) 1.43 - 07 1.68 - 09
Nearest meat animal (0.60 mi SSE) 2.53 - 07 1.75 - 09 Nearest milk cow (1.50 NE) 1.09 - 07 8.71 - 10
- Calculated using the methodology of NRC Regu latory Guide 1.111, Revision 1, July 1977.
KEY: l.ll - 06 = 1.11 x 10
-6
BYRON-UFSAR 11.3-33 TABLE 11.3-9 BYRON-EXPECTED INDIVID UAL DOSES FROM G ASEOUS EFFLUENTS DOSE RATE (mrem/yr)
LOCATION PATHWAY TOTAL BODY SKIN THYROID BONE LIVER LUNG GI-LLI Nearest Residence Plume 0.023 0.073 (0.3 mi ESE) Ground Deposition 0.057 0.067 Inhalation Adult 0.030 0.048 0.004 0.030 0.032 0.030 Teen 0.031 0.053 0.00 5 0.031 0.033 0.031 Child 0.027 0.054 0.007 0.028 0.029 0.027 Infant 0.016 0.040 0.005 0.016 0.017 0.016 Nearest Garden Leafy Vegetables (0.6 mi SW) Adult 0.006 0.028 0.002 0.00 6 0.006 0.006 Teen 0.004 0.023 0.00 2 0.004 0.004 0.004 Child 0.005 0.033 0.004 0.005 0.005 0.005 Stored Vegetables Adult 0.083 0.081 0.033 0.084 0.079 0.081 Teen 0.103 0.102 0.05 7 0.108 0.100 0.101 Child 0.169 0.171 0.138 0.180 0.167 0.167 Nearest Meat Meat Animal Adult 0.019 0.023 0.016 0.01 9 0.019 0.019 (0.6 mi SSE) Teen 0.013 0.016 0.014 0.013 0.013 0.013 Child 0.017 0.021 0.025 0.017 0.016 0.016 Nearest Milk Cow Milk (1.5 mi NE) Adult 0.027 0.102 0.012 0.02 7 0.025 0.025 Teen 0.037 0.164 0.02 4 0.040 0.036 0.035 Child 0.062 0.321 0.059 0.069 0.061 0.060 Infant 0.099 0.730 0.113 0.115 0.099 0.097 BRAIDWOOD-UFSAR 11.3-34 REVISION 5 - DECEMBER 1994 TABLE 11.3-7 COMPARISON OF MAXIMU M OFFSITE AIRBORNE CONCENTRATIONS WITH 10 CFR 20 LIMITS
- 0.30 mi NW /Q = 8.10 x 10
-7 sec/m 3 ** Limits used are those that were in effect at the time of the analysis.
KEY: 2.6 - 11 = 2.6 x 10-11 MAXIMUM SITE ANNUAL RELEASE BOUNDARY 3 10 CFR 20
- FROM ONE UNIT CONCENTRATION CONCENTRATION ISOTOPE (Ci/yr)
(µCi/ml) (µCi/ml) H 3 1.0+03 2.6-11 2.0-07 C 14 8.0+00 2.0-13 1.0-07 Ar 41 2.5+01 6.4-13 4.0-08 Kr 85m 5.0+00 1.3-13 1.0-07 Kr 85 7.0+02 1.8-11 3.0-07 Kr 87 1.0+00 2.6-14 2.0-08 Kr 88 8.0+00 2.1-13 2.0-08 Xe 131m 4.0+01 1.0-12 4.0-07 Xe 133m 1.6+01 4.1-13 3.0-07 Xe 133 2.0+03 5.1-11 3.0-07 Xe 135 1.5+01 3.9-13 1.0-07 Xe 138 1.0+00 2.6-14 3.0-08 I 131 5.4-02 1.4-15 1.0-10 I 132 3.7-03 9.5-17 3.0-09 I 133 7.2-02 1.8-15 4.0-10 Cr 51 5.3-08 1.4-21 8.0-08 Mn 54 4.7-03 1.2-16 1.0-09 Fe 55 7.0-07 1.8-20 3.0-08 Fe 59 1.6-03 4.1-17 2.0-09 Co 58 1.6-02 4.1-16 2.0-09 Co 60 7.3-03 1.9-16 3.0-10 Ni 63 7.0-07 1.8-20 2.0-09 Sr 89 3.4-04 8.7-18 3.0-10 Sr 90 6.2-05 1.6-18 3.0-11 Y 91 1.5-09 3.9-23 1.0-09 Mo 99 3.5-07 9.0-21 7.0-09 Tc 99m 2.1-09 5.4-23 5.0-07 Te 132 1.5-07 3.9-21 4.0-09 Cs 134 4.7-03 1.2-16 4.0-10 Cs 136 1.9-07 4.9-21 6.0-09 Cs 137 7.8-032.0-165.0-10 BRAIDWOOD-UFSAR 11.3-35 TABLE 11.3-8
ATMOSPHERIC DILUTION FACTORS USED IN DETERMINING OFFSITE DOSES
/Q 4 D/Q* LOCATION (sec/m
- 3) (l/m 2) Nearest site boundary (0.30 mi NW) 8.10 - 07 4.36 - 09
Nearest residence (0.30 mi NW) 8.10 - 07 4.36 - 09 Nearest garden (0.30 mi NW) 8.10 - 07 4.36 - 09
Nearest meat animal (1.70 mi NW) 7.73 - 08 4.49 - 10
Nearest milk cow (1.7 mi WSW) 7.79 - 07 3.70 - 10 Nearest milk goat (4.1 mi E) 3.43 - 08 1.49 - 10
- Calculated using the methodology of NRC Regu latory Guide 1.111, Revision 1, July 1977.
KEY: 8.10 - 07 = 8.10 x 10-7 BRAIDWOOD-UFSAR
11.3-36
REVISION 3 -
DECEMBER 1991 TABLE 11.3-9
BRAIDWOOD-EXPECTED I NDIVIDUAL DOSES FROM GASEOUS EFFLUENTS
DOSE RATE (mrem/yr)
LOCATION PATHWAY TOTAL BODY SKIN THYROID BONE LIVER LUNG GI-LLI Nearest Residence Plume 0.023 0.074 (0.3 mi NW) Ground Deposition 0.039 0.046 Inhalation Adult 0.035 0.054 0.004 0.035 0.037 0.035 Teen 0.036 0.059 0.00 5 0.036 0.038 0.036 Child 0.032 0.060 0.007 0.032 0.034 0.032 Infant 0.019 0.044 0.005 0.019 0.020 0.019 Nearest Garden Leafy Vegetables (0.3 mi NW) Adult 0.035 0.090 0.012 0.03 5 0.034 0.034 Teen 0.025 0.072 0.01 2 0.025 0.024 0.024 Child 0.031 0.102 0.022 0.031 0.030 0.030 Stored Vegetables Adult 0.498 0.491 0.173 0.500 0.488 0.491 Teen 0.622 0.619 0.29 8 0.634 0.614 0.616 Child 1.025 1.029 0.727 1.053 1.019 1.018 Nearest Meat Meat Animal Adult 0.006 0.007 0.005 0.00 6 0.006 0.006 (1.7 mi NW) Teen 0.004 0.005 0.004 0.004 0.004 0.004 Child 0.005 0.006 0.008 0.005 0.005 0.005
BRAIDWOOD-UFSAR 11.3-37 TABLE 11.3-9 (Cont'd)
DOSE RATE (mrem/yr)
LOCATION PATHWAY TOTAL BODY SKIN THYROID BONE LIVER LUNG GI-LLI Nearest Milk Cow Milk (1.7 mi WSW) Adult 0.020 0.051 0.008 0.02 0 0.019 0.019 Teen 0.028 0.081 0.01 6 0.029 0.027 0.027 Child 0.047 0.155 0.040 0.050 0.047 0.046 Infant 0.075 0.339 0.077 0.082 0.075 0.075 Nearest Milk Goat Milk (4.1 mi E) Adult 0.018 0.032 0.004 0.01 8 0.017 0.017 Teen 0.024 0.049 0.00 8 0.026 0.023 0.023 Child 0.039 0.091 0.020 0.043 0.039 0.038 Infant 0.061 0.188 0.038 0.068 0.061 0.060
B/B-UFSAR 11.3-38 REVISION 2 - DECEMBER 1990 TABLE 11.3-10 EXHAUST STACK AI RFLOW TABULATION CASE 1 CASE 2 REFUELING EXCEPTNORMAL PLANT MINI-FLOW (cfm) OPERATION (cfm) UNIT 1 Auxiliary Building Exhaust 135,980 135,980 Laboratory System Exhaust 14,430 (Byron) 14,430 (Byron) 13,030 13,030 (Braidwood) (Braidwood)
Off Gas System Steam Jet Air Ejector 0 32 Gland Steam Condenser Exhaust0 1,400 Containment Purge System Mini-Purge Exhaust (3000 CFM)0 0
Main-Purge Exhaust 43,900 0 194,310 (Byron) 151,842 (Byron) 192,910 150,442 (Braidwood) (Braidwood) UNIT 2 Auxiliary Building Exhaust 135,980 135,980 Auxiliary Building Filtered Vents 1,000 1,000 Solid Radwaste Area Exhaust 8,630 8,630 Off Gas System Steam Jet Air Ejector 0 32 Gland Steam Condenser Exhaust 0 1,400 Containment Purge System Mini-Purge Exhaust (3000 CFM)0 0
Main-Purge Exhaust 43,900 0 189,510 147,042
BYRON-UFSAR
11.4-52 REVISION 7 - DECEMBER 1998 TABLE 11.4-1 SOLID WASTE MANAGEME NT SYSTEM EQUIPMENT AND STORAGE DESI GN CAPACITIES
PROCESSING EQUIPMENT QUANTITYDESIGN CAPACITY MATERIALS Decanting tank 2 500 gallons 304L SS Decanting pump 2 18 gpm 304L SS
Metering pump 4 15 gpm 304L SS
Cement storage tank 1 1000 ft 3 CS Drum processing unit 2 1 Drum 304L SS Packaging container (drum) - 55 gallons CS Packaging container (liner)- Up to 200 ft 3 CS or Polyethylene
Dry waste compactor 1 1 Drum CS
Traveling bridge crane 1 1 9.3 tons CS Fixed bridge crane 1 2 1.0 ton CS Drum transfer car 2 2 2 drums CS Startup heater 1 395 scfm 304SS/
347SS
Air heater 1 320 scfm 304SS/
316L-SS Gas heater 1 786 scfm 304SS/
Fluid bed dryer air blower 1 317 scfm CS
Dry waste processor air blower 1 300 scfm CS
BYRON-UFSAR
11.4-53 TABLE 11.4-1 (Cont'd)
PROCESSING EQUIPMENT QUANTITYDESIGN CAPACITY MATERIALS Waste feed filter 1 30 gpm 316L-SS FBD inlet air filter 1 320 scfm CS
DWP inlet air filter 1 300 scfm CS
Gas filter assembly 2 466 scfm CS
Recirculating gas filter 1 320 scfm CS
Caustic tank 1 1000 gal 304SS Decon tank 1 650 gal 304SS Contaminated oil tank 1 150 gal CS
Bed storage and transfer hopper 2 2900 lb 304SS
Trash hopper 2 1500 lb CS/Fe
Waste liquor storage tank 2 3500 gal 316L-SS Fluid bed dryer 1 0.41 gpm 347SS/ Inconel 625
Dry waste processor 1 83 lb/hr 347SS
Trash conveyor 1 --- Rubber/CS
Trash elevator 1 20 lb/min CS
Waste feed pump 1 120 gph 316L-SS Waste recirc. pump 2 500 gpm 316L-SS Decon. pump 1 50 gpm 304SS
Dryer feed pump 1 30 gph 316L-SS Condensate pump 1 22 gpm 316SS
Contaminated oil pump 1 14 gpm CS Scrubber preconcentrator recirc. pump 1 20 gpm 316L-SS
Caustic additive pump 2 15 gpm 304SS
BYRON-UFSAR
11.4-54 TABLE 11.4-1 (Cont'd)
PROCESSING EQUIPMENT QUANTITY DESIGN CAPACITY MATERIALS Scrubber preconcentrator 1 16.8 gpm 316L-SS/ Inconel 625 Secondary scrubber 1 1142 scfm 316L-SS Condenser 1 22 gpm 316SS Metal detector 1 1 Trash Bag Al,Cu Volume reduction system 1 911 scfm 347SS gas/solids separator Trash shredder 1 20 lb/min Fe/CS/CrMo Steel Polymer storage tank 2 3000 gal 304L Promoter additive 1 6 gal 304 storage tank Isolation hopper 1 7.5 ft 3 316L-SS Storage hopper 1 80 ft 3 304L-SS Drum processing 1 1 drum 304L enclosure Flame arrester 2 --- --- Volume reduction system 1 250 scfm 304L solidification system gas/solid separator Volume reduction product 1 250 scfm SA285 Gr. C blower Polymer circulating pump 1 15gpm/7.5gpm 316SS Promoter metering pump 1 10oz/min 420SS Roller conveyor 1 30 fpm CS Polymer filter 1 65 gpm 304SS Polymer station vent filter1 75 scfm 304SS Volume reduction solidi- 1 180 scfm 304L fication system product blower filter
BYRON-UFSAR
11.4-55 REVISION 7 - DECEMBER 1998 TABLE 11.4-1 (Cont'd)
STORAGE AREA NUMBER OF STORAGE AREAS DESIGN CAPACITY PER STORAGE AREA Low level 1 500 drums or 30 containers
Intermediate level 1 640 drums or 30 containers
Dry compacted waste 1 70 drums
Dry uncompacted waste 1 90 ft 3
Empty drum or container 2 100 drums or 6 containers (total)
NOTES 1. Overhead Crane Operating Speeds High-Speed Low-Speed
Bridge 125 fpm 2.5 fpm
Trolley 125 fpm 2.5 fpm
Drum Grab Hoist 30 fpm 7.5 fpm
- 2. Drum Transfer Car Operating Speeds High-Speed Low-Speed
100 fpm 10 fpm
BYRON-UFSAR
11.4-56
REVISION 7 - DECEMBER 1998 TABLE 11.4-2 EXPECTED AND DESIGN BASIS ANNUAL VOLUMES OF (UNITS 1 AND 2)
SOLID WASTE MANAGEME NT SYSTEM OUTPUT*
Solid waste processed by the solid r adwaste management system and quant ities of processed was te requiring onsite storage or offsi te disposal EXPECTED NUMBER OF DESIGN NUMBER OF TYPE OF WASTE VOLUMES CONTAINERS VOLUME CONTAINERS Deep Bed Resin 1,600 ft 3 2,393 drums 1,600 ft 3 2,393 drums or 10 liners or 10 liners Disposable Filter Elements 75 ft 3 190 drums 75 ft 3 190 drums or 2 liners or 2 liners Sludges and Liquids*** 16,850 ft 3 4,580 drums 18,690 ft 3 5,140 drums Dry Active Waste 36,220 ft 3 580** drums 36,220 ft 3 1,160** drums 73 boxes 73 boxes Total 54,745 ft 3 7,743 drums, 56,585 ft 3 8,883 drums, 73 boxes 73 boxes or 12 liners, or 12 liners, 5,350 drums 6,490 drums and 73 boxes and 73 boxes
___________________
- The values given are approxi mate. The actual data a re available in the effluent release reports, which a re prepared in accorda nce with the ODCM. ** Not solidified. *** Sludges and liqu ids are normally processed in the liquid radwaste system.
BYRON-UFSAR
11.4-57
REVISION 6 - DECEMBER 1996 TABLE 11.4-3
PLANT INTERFACES WITH SOLID RADWASTE SYSTEM ESTIMATED ESTIMATED GROSS INTERFACE NUMBER LINE* LINE EXPECTED TEMPERATURE EXPECTED ESTIMATED RADIOISOTOPE AND DESCRIPTION NUMBER SIZE PRESSURE (°F) FLOW RATE BATCH SIZE CONCENTRATION**** 1. Spent Resin OWXX9A 1-1/2 in. 50 psig 90 120 gpm up to 400 gal 370 Ci/cc
- 2. Evaporator Concentratesf OWX143BA 1-1/2 in. 35 psig 130-90 15 gpm 22.5-36.5 gal** 0.05 Ci/cc
- 3. Flush and Decontamination OWX146BA 1-1/2 in. 52 psig 110 50 gpm 25 gal 0.16 Ci/cc
- 4. Volume Reduction System***
- a. Evaporator concentrates OVR80A 1-1/2 in. 35 psig 190 30 gpm 3500 gal 0.05 Ci/cc
- b. Waste oil OVR69A 2 in. 25 psig 150 50 gpm 140 gal low
- Typical line numbers, for Unit B line numbers the last letter is B.
- Directly to the drum from a recirculation loop via a metering pump.
- Byron does not operate the volume reduction system.
- Based on Table 11.1-11.
f Evaporator concentrates are normally processed in the liquid radwaste system.
BYRON-UFSAR
11.4-58 TABLE 11.4-3 (Cont'd)
ESTIMATED ESTIMATED GROSS INTERFACE NUMBER LINE* LINE EXPECTED TEMPERATURE EXPECTED ESTIMATED RADIOISOTOPE AND DESCRIPTION NUMBER SIZE PRESSURE (°F) FLOW RATE BATCH SIZE CONCENTRATION**** c. Pump seals/dilution OPW60A 2 in. 50 psig 120 75 gpm continuous Primary water intermittent
- d. Decon water supply OPMK7A 2 in. 135 psig 100 100 gpm 600 gal Primary
- e. Cooling water supply OWSJ4A 4 in. 140 psig 110 156 gpm continuous 0.0
- f. Cooling water return OWSJ6A 3 in. 140 psig 124 156 gpm continuous 0.0
- g. Service air supply 2SA67A 1-1/2 in. 115/90 psig 120 78 scfm continuous 0.0
- h. Filtered exhaust OVR084B 6 in. 2 in. H 2O 175 477 scfm continuous 5.6 x 10
-4 Ci/cc
- i. Drains OWF69A 3 in. 50 psig 150 50 gpm intermittent 2.7 x 10
-2 Ci/cc j. Decon water return OVR123A 2 in. 50 psig 180 50 gpm 150 gal 0.05 Ci/cc
- k. Filter backwash inlet OVR81A 3/4 in. 150 psig 250 50 gpm 50 gal Primary water
- l. Filter backwash outlet OVR13A 3/4 in. 150 psig 200 50 gpm 50 gal 0.5 Ci/cc
- m. Instrument air OVA210A 1 in. 115 psig 150 82 scfm continuous 0.0
- n. Bed storage hopper fill OVR47A 6 in. ambient ambient gravity 50 lb 0.0
- o. Dry active water - - ambient ambient 20 ft 3/min 7.5 ft 3 Low
BYRON-UFSAR
11.4-59 RE VISION 6 - DECEMBER 1996 TABLE 11.4-3 (Cont'd)
ESTIMATED ESTIMATED GROSS INTERFACE NUMBER LINE* LINE EXPECTED TEMPERATURE EXPECTED ESTIMATED RADIOISOTOPE AND DESCRIPTION NUMBER SIZE PRESSURE (°F) FLOW RATE BATCH SIZE CONCENTRATION**** 9. Volume Reduction System***
Production Solidification System
- a. Cooling water supply OWO120A 1-1/2 in. 100 psig 100 10 gpm intermittent 0.0
- b. Cooling water return OWO128A 1-1/2 in. 100 psig 100 10 gpm intermittent 0.0
- c. Instrument air (polymer) OIA117A 1 in. 115 psig 120 5 scfm intermittent 0.0
- d. Instrument air OVR257A 1/2 in. 115 psig 120 58 scfm intermittent 0.0 (equipment)
- e. Instrument air OVR255A 1 in. 115 psig 120 58 scfm continuous 0.0 (equipment) f. Instrument air OVR256A 3/4 in. 115 psig 120 58 scfm intermittent 0.0 (storage hopper)
- g. Instrument air (blower) OVR258A 1 in. 115 psig 120 60 scfm intermittent 0.0
- h. Drain (drum processing) OVR169A 3 in. 4 psig 180 20 gpm intermittent Low
- i. Drain (storage hopper) OVR173A 2 in. 4 psig 180 15 gpm intermittent 8.4 x 10
-2 Ci/cc
- j. Drain (surge hopper) OVR181A 1-1/2 in. 4 psig 180 5 gpm intermittent 8.4 x 10
-2 Ci/cc
- k. Polymer filling ------- 2 in. -1 in. H 2O ambient 10 scfm continuous 0.0 station vent
- l. Blower discharge OVR180A 2-1/2 in. 0.5 psig 120 60 scfm intermittent Low
B/B-UFSAR
11.4-60 through 11.4-63 REVISION 6 - DECEMBER 1996
Pages 11.4-60 through 11.4-63 have been deleted intentionally.
BRAIDWOOD-UFSAR
11.4-64 REVISION 12 - DECEMBER 2008 TABLE 11.4-1 SOLID WASTE MANAGEME NT SYSTEM EQUIPMENT AND STORAGE DESI GN CAPACITIES
PROCESSING EQUIPMENT QUANTITY DESIGN CAPACITY MATERIALS Packaging container - up to 200 ft 3 CS or (liner) polyethylene Packaging container (drum) - 55 gal CS Traveling bridge crane 1 1 9.3 tons CS Fixed bridge crane 1 2 1.0 ton CS Drum transfer car 2 2 2 drums CS Cartridge filter transfer vehicle 3 1 1 drum CS
NOTE: Processing equipment for the volume reduction and radwaste solidification systems has been intentio nally deleted from this table. Braidwo od station does not intend to use this equipment.
BRAIDWOOD-UFSAR
11.4-65 REVISION 9 - DECEMBER 2002 TABLE 11.4-1 (Cont'd)
Page 11.4-65 has bee n deleted intentionally.
BRAIDWOOD-UFSAR
11.4-66 REVISION 9 - DECEMBER 2002 TABLE 11.4-1 (Cont'd)
Page 11.4-66 has bee n deleted intentionally.
BRAIDWOOD-UFSAR
11.4-67 REVISION 7 - DECEMBER 1998 TABLE 11.4-1 (Cont'd)
NUMBER OF DESIGN CAPACITY STORAGE AREA STORAGE AREAS PER STORAGE AREA Low level 1 500 drums or 30 containers
Intermediate level 1 640 drums or 30 containers
Dry compacted waste 1 70 drums
Dry uncompacted waste 1 90 ft 3 Empty drum or container 2 100 drums or 6 containers (total)
NOTES 1. Overhead Crane Operating Speeds High-Speed Low-Speed Bridge 125 fpm 2.5 fpm Trolley 125 fpm 2.5 fpm
Drum Grab Hoist 30 fpm 7.5 fpm
- 2. Drum Transfer Car Operating Speeds High-Speed Low-Speed 100 fpm 10 fpm
- 3. Cartridge Filter Transfer Vehicle Operating Speeds Variable
0 fpm to 250 fpm
BRAIDWOOD-UFSAR
11.4-68
REVISION 7 - DECEMBER 1998 TABLE 11.4-2 EXPECTED AND DESIGN BASIS ANNUAL VOLUMES OF (UNITS 1 AND 2)
SOLID WASTE MANAGEME NT SYSTEM OUTPUT*
Solid waste processed by the solid r adwaste management system and quant ities of processed waste requiring onsite storage or of fsite disposal
EXPECTED NUMBER OF DESIGN NUMBER OF TYPE OF WASTE VOLUMES CONTAINERS VOLUME CONTAINERS Deep Bed Resin 1,600 ft 3 10 liners 1,600 ft 3 10 liners Disposable Filter Elements 75 ft 3 2 liners 75 ft 3 2 liners Sludges and Liquids*** 16,850 ft 3 141 liners 18,690 ft 3 156 liners Dry Active Waste 36,220 ft 3 580 drums** 36,220 ft 3 1,160 drums** 73 boxes 73 boxes Total 54,745 ft 3 153 liners 56,585 ft 3 168 liners 580 drums 1,160 drums 73 boxes 73 boxes
___________________
- The values given are approxi mate. The actual data are available in the effluent release reports, which are p repared in accordance with the ODCM. ** Not solidified.
- Sludges and liquids are no rmally processed in the liquid radwaste system.
BRAIDWOOD-UFSAR
11.4-69
REVISION 6 - DECEMBER 1996 TABLE 11.4-3
PLANT INTERFACE WITH SOLID RADWASTE SYSTEM
ESTIMATED ESTIMATED GROSS INTERFACE NUMBER LINE* LINE EXPECTED TEMPERATURE EXPECTED ESTIMATED RADIOISOTOPE AND DESCRIPTION NUMBER SIZE PRESSURE (°F) FLOW RATE BATCH SIZE CONCENTRATION** 1. Spent Resin OWX425A 1-1/2 in. 75 psig 90 40 gpm up to 845 gal 1500 Ci/cc
- 2. Evaporator Concentrates*** OWXZ9D 1-1/2 in. 109 psig 130-190 45 gpm 100 gal 0.05 Ci/cc
- 3. Resin Flush and Decontamination OWX137A 2 in. 50 psig 120 50 gpm 115 gal 0.16 Ci/cc
- 4. Pump Seals
- a. Evaporator concentrates OWX530AA 1/2 in. 5 psig ambient .25 gpm intermittent Low
- b. Spent resin OWX589CA 3/8 in. 90 psig 120 .25 gpm intermittent Primary water
- 5. Volume Reduction Systemf
- a. Waste oil OVR69A 2 in. 25 psig 150 50 gpm 140 gal low
- b. Pump seals/dilution water OWMK7A 2 in. 135 psig 100 75 gpm continuous 0.0 intermittent
- c. Decon water supply OWMK7A 2 in. 135 psig 100 100 gpm 600 gal 0.0
- Typical line numbers, for Unit B line numbers the last letter is B.
- Based on Table 11.1-11. *** Evaporator concentrates are normally processed in the liquid radwaste system. f Braidwood does not operate the volume reduction system.
BRAIDWOOD-UFSAR
11.4-70
REVISION 6 - DECEMBER 1996 TABLE 11.4-3 (Cont'd)
ESTIMATED ESTIMATED GROSS INTERFACE NUMBER LINE* LINE EXPECTED TEMPERATURE EXPECTED ESTIMATED RADIOISOTOPE AND DESCRIPTION NUMBER SIZE PRESSURE (°F) FLOW RATE BATCH SIZE CONCENTRATION** d. Cooling water supply OWSJ4A 4 in. 140 psig 110 156 gpm continuous 0.0
- e. Cooling water supply OWSJ6A 3 in. 140 psig 124 156 gpm continuous 0.0
- f. Filtered exhaust OVR084B 4 in. 2 in. H 2O 175 477 scfm continuous 5.6x10
-4 Ci/cc
- g. Drains OWF69A 3 in. 50 psig 150 50 gpm intermittent 2.7x10
-2 Ci/cc
- h. Decon water supply OVR123A 2 in. 50 psig 180 50 gpm 150 gal 0.05 Ci/cc
- i. Filter backwash inlet OVR81A 3/4 in. 150 psig 250 50 gpm 50 gal Primary water
- j. Filter backwash outlet OVR13A 3/4 in. 150 psig 200 50 gpm 50 gal 0.5 Ci/cc
- k. Instrument air OVR210A 1 in. 115 psig 150 82 scfm continuous 0.0 l. Bed storage hopper fill OVR47A 6 in. ambient ambient gravity 50 lb Low
- m. Dry active waste - - ambient ambient 20 ft 3/min 7.5 ft 3 Low
- 6. Volume Reduction Systemf Production Solidification System
- a. Cooling water supply OWO348A 1-1/2 in. 100 psig 100 10 gpm intermittent 0.0
- b. Cooling water return OWO349A 1-1/2 in. 100 psig 100 10 gpm intermittent 0.0
- c. Instrument air (polymer) OIA116A 1 in. 115 psig 120 5 scfm intermittent 0.0
BRAIDWOOD-UFSAR
11.4-71 TABLE 11.4-3 (Cont'd)
ESTIMATED ESTIMATED GROSS INTERFACE NUMBER LINE* LINE EXPECTED TEMPERATURE EXPECTED ESTIMATED RADIOISOTOPE AND DESCRIPTION NUMBER SIZE PRESSURE (°F) FLOW RATE BATCH SIZE CONCENTRATION** d. Instrument air (drum processing) OVR257A 1/2 in. 115 psig 120 58 scfm intermittent 0.0
- e. Instrument air (equipment) OVR255A 1 in. 115 psig 120 58 scfm continuous 0.0
- f. Air bump (surge hopper) OVR307A 3/8 in. 40 psig 120 58 scfm intermittent 0.0
- g. Instrument air (storage hopper) OVR256A 3/4 in. 115 psig 120 58 scfm intermittent 0.0
- h. Air bump (storage hopper) OVR310A 3/8 in. 40 psig 120 58 scfm intermittent 0.0
- i. Instrument air (blower) OVR258A 1 in. 115 psig 120 60 scfm intermittent 0.0
- j. Drain (drum processing) OVR169A 3 in. 4 psig 180 20 gpm intermittent Low
- k. Drain (storage hopper) OVR173A 2 in. 4 psig 180 15 gpm intermittent 8.4x10
-2 Ci/cc
- l. Drain (surge hopper) OVR181A 1-1/2 in. 4 psig 180 5 gpm intermittent 8.4x10
-2 Ci/cc
- m. Polymer filling station vent ----- 2 in. -1 in. H 2O ambient 10 scfm continuous 0.0
- n. Blower discharge OVR180A 2-1/2 in. 0.5 psig 120 60 scfm intermittent Low
BRAIDWOOD-UFSAR
11.4-72 TABLE 11.4-3 (Cont'd)
ESTIMATED ESTIMATED GROSS INTERFACE NUMBER LINE* LINE EXPECTED TEMPERATURE EXPECTED ESTIMATED RADIOISOTOPE AND DESCRIPTION NUMBER SIZE PRESSURE (°F) FLOW RATE BATCH SIZE CONCENTRATION** 7. Vendor Supplied Mobile Radwaste System
- a. Instrument air O1A117A 3/4 in. 115 psig 120 50 scfm continuous 0.0
- b. Service air OSAR1A 3/4 in. 115 psig 120 50 scfm continuous 0.0
- c. Demineralized water OWMT2A 2 in. 135 psig 100 100 gpm intermittent 0.0
- d. Service water supply OWS59A 2 in. 140 psig 96 25 gpm continuous 0.0
- e. Service water return OWSX5A 2 in. 140 psig 96 25 gpm continuous 0.0
- f. Drain OWX439A 2 in. 100 psig 100 25 gpm continuous 0.16 Ci/cc
- g. Vent OVF075A 4 in. 3 psig 175 200 scfm continuous Low
BYRON/BRAIDWOOD STATIONS UPDATED FINAL SAFETY ANALYSIS REPORT FIGURE 11.3-2 GASEOUS WASTE PROCESSING SYSTEM FLOW DIAGRAM CARTRIDGE DRY ACTIVE FILTERS WASTES SLUDGES AND LIQUIDS LOW ACTMTY SPENT RESIN REVISION 6 DECEMBER 1996 HIGH ACTMTY SPENi RESIN HIGH ACTIVITY SPENT RESIN STORAGE TANK PACKAGE STORAGE AREA COMPACTOR PACKAGE SPENT RESIN.STORAGE TANK MOBILE t AUX.BLOC.MOBILE LINER STORAGE RADWASTE RADWASTE AREA , SYSTEM FLOOR DRAINS SYSTEM I UNER UNER STORAGE AREA TRUCK TRUCK TRUCK DISPOSAL SITE BRAIDWOOD STATION UPDATED FINAL SAFETY ANALYSIS REPORT FIGURE 11.4-1 RADWASTE DISPOSAL SYSTEM FLOW DIAGRAM CARTRIDGE DRY ACTIVE FILTERS WASTES SLUDGES AND LIQUIDS LOW ACTIVITY SPENT RESIN REVISION 6 DECEMBER 1996 HIGH ACTIVITY SPENT RESIN PACKAGE STORAGE AREA LINER TRUCK COMPACTOR PACKAGE STORAGE AREA TRUCK MOBILE RADWASTE SYSTEM LINER t AUX.BLOC.FLOOR ORAINS SPENT RESIN STORAGE TANK MOBILE RADWASTE SYSTEM LINER STORAGE AREA TRUCK DISPOSAL SITE BYRON STATION UPDATED FINAL SAFElY ANALYSIS REPORT FIGURE 11,4-1 RADWASTE DISPOSAL SYSTEM FLOW DIAGRAM
B/B-UFSAR 11.0-i REVISION 9 - DECEMBER 2002 CHAPTER 11.0 -
RADIOACTIVE WASTE MANAGEMENT TABLE OF CONTENTS PAGE 11.0 RADIOACTIVE WASTE MANAGEMENT 11.1-1 11.1 SOURCE TERMS 11.1-1 11.1.1 Definition of Radioactive Source Terms 11.1-1 11.1.1.1 Design-Basis Shi elding Source Terms 11.1-1 11.1.1.2 Realistic Source Terms 11.1-1 11.1.1.3 Accident Sources 11.1-1 11.1.2 Basis for Radioactive Source Terms 11.1-2 11.1.2.1 Conservative Mod el for React or Coolant Activity 11.1-2 11.1.2.2 Realistic Model for Reactor Coolant Activity 11.1-3 11.1.3 Source Terms for Shielding Design Basis 11.1-4 11.1.4 Source Terms for Component Failure 11.1-5 11.1.5 Source Terms for Radwaste System Components 11.1-5 11.1.6 Sources of I n-Plant Airborne R adioactivity 11.1-5 11.1.7 Sources of Radio active Releases to the Environment 11.1-6 11.1.7.1 Gaseous Releases 11.1-6 11.1.7.2 Liquid Releases 11.1-6 11.1.8 Impact of Uprate on No rmal Operation Radiation Source Terms 11.1.9 References 11.1-6 11.2 LIQUID WASTE MANAGEMENT SYSTEMS 11.2-1 11.2.1 Design Bases 11.2-1 11.2.1.1 Safety Design Basis 11.2-1 11.2.1.2 Power Generation Design Basis 11.2-1 11.2.1.3 Expected Radioactive Releases 11.2-2 11.2.1.4 10 CFR 50 Comparison 11.2-2 11.2.1.5 10 CFR 20 Comparison 11.2-2a 11.2.1.6 Component Specifications 11.2-2a 11.2.1.7 Seismic Design and Quality Group 11.2-3 11.2.1.8 Facility and Equipment Design 11.2-3 11.2.1.8.1 Maintenance Operations 11.2-3 11.2.1.8.2 Floor, Wall, and Ceiling Coatings 11.2-3 11.2.1.9 Tank Level Control 11.2-3 11.2.1.10 Prevention of Un controlled Releases 11.2-4 11.2.1.11 ETSB-BTP 11-1 Comparison 11.1-5 11.2.2 System D escription 11.2-5 11.2.2.1 Steam Generator Blowdown Subsystem 11.2-6 11.2.2.1.1 Normal Operation 11.2-7 11.2.2.1.2 Circulating Water to Sec ondary System Leakage 11.2-8 11.2.2.1.3 Primary-to-Secon dary Leakage Concurrent with Failed Fuel 11.2-8
B/B-UFSAR 11.0-ii REVISION 7 - DECEMBER 1998 TABLE OF CONTENTS (Cont'd)
PAGE 11.2.2.1.4 Primary-to-Sec ondary Leakage Not Concurrent with Failed Fuel 11.2-8 11.2.2.1.5 Transient Operating Conditions 11.2-9 11.2.2.2 Nonblowdown Liquid Radwaste Subsystem 11.2-9 11.2.2.2.1 Auxiliary Building Equipment Drain 11.2-10 11.2.2.2.2 Auxiliary Building Floor Drain 11.2-11 11.2.2.2.3 Chemical Waste Drain 11.2-11
11.2.2.2.4 Regeneration Waste Drain 11.2-12 11.2.2.2.5 Laundry Drain 11.2-12 11.2.2.2.6 Turbine Building Equipment Drain 11.2-12 11.2.2.2.7 Turbine Building Floor Drain 11.2-13 11.2.2.2.8 Turbine Building Fire and Oil Sump 11.2-13 11.2.2.2.9 Condensate Polisher Sump 11.2-13 11.2.2.2.10 Waste Treatment System 11.2-13 11.2.2.3 Operating Procedures 11.2-14 11.2.2.4 Performance Tests 11.2-14 11.2.2.5 Control and Instrumentation 11.2-14 11.2.3 Radioactive Releases (Byron) 11.2-15 11.2.3.1 Release Points (Byron) 11.2-15 11.2.3.2 Dilution Factors (Byron) 11.2-15 11.2.3.3 Estimated Annual Average Doses (Byron) 11.2-15 11.2.3 Radioactive Releases (Braidwood) 11.2-16 11.2.3.1 Release Points (Braidwood) 11.2-16 11.2.3.2 Dilution Factors (Braidwood) 11.2-16 11.2.3.3 Estimated Annual Average Doses (Braidwood) 11.2-16 11.2.4 References 11.2-17 11.3 GASEOUS WASTE MANAGEMENT SYSTEMS 11.3-1 11.3.1 Design Bases 11.3-1 11.3.2 System D escription 11.3-2 11.3.2.1 System Design 11.3-2 11.3.2.2 Component Design 11.3-4 11.3.2.3 Instrumentation Design 11.3-4 11.3.2.4 Operating Procedure 11.3-5 11.3.2.5 Operations 11.3-5 11.3.2.6 Refueling 11.3-7 11.3.2.7 Auxiliary Services 11.3-7 11.3.2.8 Performance Tests 11.3-7 11.3.3 Radioactive Releases 11.3-8 11.3.3.1 NRC Requirements 11.3-8 11.3.3.2 Westinghouse PWR Experience Releases 11.3-8 11.3.3.3 Expected Gaseo us Waste Processing System Releases 11.3-8
B/B-UFSAR 11.0-ii (Cont'd)
REVISION 2 - DECEMBER 1990 TABLE OF CONTENTS (Cont'd)
PAGE 11.3.3.4 Estimated Total Releases 11.3-9 11.3.3.5 Effluent Concentrations and Dilution Factors 11.3-9 11.3.3.6 Release Points of Dilution Factors 11.3-9 11.3.3.7 Estimated Doses from Gaseous Releases 11.3-10 11.3.4 References 11.3-10
B/B-UFSAR 11.0-iii REVISION 12 - DECEMBER 2008 TABLE OF CONTENTS (Cont'd)
PAGE 11.4 SOLID WASTE MA NAGEMENT SYSTEM 11.4-1 11.4.1 Design Bases 11.4-1 11.4.1.1 Power Generation Design Bases 11.4-1 11.4.1.2 Safety Design Bases 11.4-1 11.4.1.3 Type of Waste 11.4-2 11.4.1.4 Expected Volumes and Isotopic Compositions 11.4-3 11.4.1.5 ETSB-BTP 11-3 Comparison 11.4-3 11.4.1.6 Comparison of Processing Capacity and Design Basis Waste Volumes (Byron) 11.4-4 11.4.1.6 Comparison of Proces sing Capacity and Design Basis Waste Volumes (Braidwood) 11.4-5 11.4.1.7 Solid Radwaste System Monitoring 11.4-7 11.4.2 System D escription 11.4-7 11.4.2.1 Deleted 11.4-7 11.4.2.2 Deleted 11.4-7 11.4.2.3 Deleted 11.4-7 11.4.2.4 Drum Handling Equipment 11.4-11 11.4.2.5 Smear Test and Label Station 11.4-12 11.4.2.6 Dry Waste Compactor (Byron) 11.4-12 11.4.2.7 Storage Areas 11.4-12 11.4.2.8 Control Room 11.4-13 11.4.2.9 Deleted 11.4-13 11.4.2.10 Deleted 11.4-13 11.4.2.11 Deleted 11.4-13 11.4.2.12 System Interfaces 11.4-13 11.4.2.13 Deleted 11.4-13 11.4.3 Volume Reduction System Description 11.4-14 11.4.4 Polymer/VR Product Drumming Station 11.4-14
B/B-UFSAR 11.0-iv REVISION 4 - DECEMBER 1992 TABLE OF CONTENTS (Cont'd)
PAGE 11.5 PROCESS AND EFFL UENT RADIOLOGICAL MONITORING AND SAMPLING SYSTEMS 11.5-1 11.5.1 Design Bases 11.5-1 11.5.1.1 Design Objectives 11.5-1 11.5.1.2 Design Criteria 11.5-3 11.5.2 System D escription 11.5-5 11.5.2.1 Instrumentation 11.5-5 11.5.2.2 Airborne Process and Effluent Monitors 11.5-7 11.5.2.2.1 Auxiliary Bu ilding Vent Stack Effluent 11.5-7 11.5.2.2.2 Auxiliary Buil ding Plant Areas (for Auxiliary Building Vent Exhausts) 11.5-7 11.5.2.2.3 Pipe Tunnel (f or Auxiliary Building Vent Exhausts) 11.5-7 11.5.2.2.4 Fuel-Handling Building Exhaust 11.5-7 11.5.2.2.5 Containment Purge Effluent 11.5-8 11.5.2.2.6 Fuel-Handling Incident in the Fuel Handling Building 11.5-8 11.5.2.2.7 Fuel-Handlin g Accident in the Containment Building 11.5-8 11.5.2.2.8 Main Control Room Outside Air Intakes A and B 11.5-8 11.5.2.2.9 Main Control Room Turbine Building Air Intakes A and B 11.5-9 11.5.2.2.10 Containment Atmosphere Monitoring 11.5-9 11.5.2.2.11 Miscel laneous Tank Vent Exhaust 11.5-10 11.5.2.2.12 Radwaste Area Vent Exhaust 11.5-10 11.5.2.2.13 SJAE/Gland Steam Exhaust 11.5-10 11.5.2.2.14 Gas Decay Tank Effluent 11.5-10
B/B-UFSAR 11.0-v TABLE OF CONTENTS (Cont'd)
PAGE 11.5.2.2.15 VR Systems Areas and Cubicles Ventilation Exhaust 11.5-11 11.5.2.2.16 TSC Ventilation System 11.5-11 11.5.2.2.17 Miscel laneous Process Monitors 11.5-11 11.5.2.2.18 Auxiliary Bu ilding Vent Stack Wide Range Gas Monitor 11.5-11 11.5.2.3 Liquid Effluent Monitors 11.5-11 11.5.2.3.1 Liquid Radwaste Effluent Monitor 11.5-12 11.5.2.3.2 Component Cooling Water Monitors 11.5-12 11.5.2.3.3 Steam Generator Blowdown 11.5-12 11.5.2.3.4 Blowdown Filters 11.5-12 11.5.2.3.5 Gross Failed Fuel Monitor 11.5-12 11.5.2.3.6 Miscellaneous Process Liquid Monitors 11.5-13 11.5.2.3.7 Turbine Building Fire and Oil Sump 11.5-13 11.5.2.3.8 Condensate Cleanup Area Sumps Discharge 11.5-13 11.5.2.4 Sampling 11.5-13 11.5.2.4.1 Process Sampling 11.5-14 11.5.2.4.2 Effluent Sampling 11.5-14 11.5.2.4.3 Representative Sampling 11.5-14 11.5.2.4.4 Analytical Procedures 11.5-14 11.5.2.5 Instrument Ins pection, Calibration, and Maintenance 11.5-15 11.5.2.5.1 Calibration 11.5-16 11.5.3 Effluent Monitoring and Sampling 11.5-16 11.5.4 Process Monitori ng and Sampling 11.5-16
B/B-UFSAR 11.0-vi REVISION 9 - DECEMBER 2002 CHAPTER 11.0 -
RADIOACTIVE WASTE MANAGEMENT LIST OF TABLES NUMBER TITLE PAGE 11.1-1 Parameters Used in the Calculation of Design Basis Primary Coolant Activities - Original and Uprated (***) 11.1-7 11.1-2 Design-Basis Rea ctor Coolant Fission and Corrosion Product Activity (Original Design) 11.1-10 11.1-3 Parameters Used in the Calculation of Realistic, Opera tional Basis Primary Coolant Activities 11.1-11 11.1-4 Realistic, Ope rational Basis Reactor Coolant Fission and Corrosion Product Activities 11.1-13 11.1-5 Maximum Realisti c, Operational Basis Waste Gas Decay Tank Activity for Gas Decay Tank Rupture 11.1-15 11.1-6 Realistic Sour ce Terms for Steam Generator Blowdo wn and Radioactive Drain Streams 11.1-16 11.1-7 Realistic Source Terms for Balance of Plant 11.1-20 11.1-8 Realistic Sour ce Terms for Radwaste System Filters and Demineralizers 11.1-24 11.1-9 Realistic Source Ter ms for NSSS Filters 11.1-28 11.1-10 Realistic So urce Terms for NSSS Demineralizers 11.1-31 11.1-11 Realistic Source Terms for C oncentrates and Spent Resin Tanks (Byron) 11.1-33 11.1-11 Realistic Sour ce Terms for High and Low Activity Spent Resin Tanks (Braidwood) 11.1-35 11.1-12 Deleted 11.1-13 Uprated Design-Basis Reactor Coolant Fission And Corrosion Pr oduct Activity 11.2-1 Expected Annual Average Releases of Radionuclides in Liquid Effluents 11.2-18 11.2-2 Parameters U sed in the GALE-PWR Computer Program (Original & Uprated) - Note 1 11.2-19 11.2-3 Pathways Doses f rom Liquid Effluents (Byron) 11.2-22 11.2-3 Pathways Doses f rom Liquid Effluents (Braidwood) 11.2-23 11.2-4 Comparison of Expected Liqui d Effluent Concentrations to 10 CFR 20 Limits (Byron) 11.2-24 11.2-4 Comparison of Expected Liqui d Effluent Concentrations to 10 CFR 20 Limits (Braidwood) 11.2-25 11.2-5 Liquid Radwaste System Components and Design Parameters Per Station 11.2-26 11.2-6 Design-Basis A nnual Average and Maximum Waste Stream Flows (Two Units) 11.2-32
B/B-UFSAR 11.0-vii REVISION 6 - DECEMBER 1996 LIST OF TABL ES (Cont'd)
NUMBER TITLE PAGE 11.2-7 Design-Basis P rocess Decontamination Factors 11.2-33 11.2-8 Consumption Fa ctors for the Maximum Exposed Individual 11.2-35 11.2-9 Summary of T ank Level Indicati on, Annunciators, and Overflows for Tanks Outside of Containment Poten tially Containing Radioactive Liquids 11.2-36 11.3-1 Gaseous Wast e Processing System Component Data 11.3-11 11.3-2 Gaseous Wast e Processing System Instrumentation Design Parameters 11.3-12 11.3-3 Process Paramete rs and Realistic, Operation Basis Activities in Gaseous Waste System 11.3-15 11.3-4 Assumptions Used in Calculating Expected System Activities 11.3-23 11.3-5 Typical Gase ous Releases From Operating Reactors 11.3-25 11.3-6 Expected Annual Average Release of Airborne Radionuclides 11.3-26 11.3-7 Comparison of Maximum Offsite Airborne Concentrations with 10 CFR 20 Limits (Byron) 11.3-30 11.3-8 Atmospheric Dilution Factors Used in Determining Offsite Doses (Byron) 11.3-31 11.3-9 Byron - Expected Individual Doses from Gaseous Effluents 11.3-32 11.3-7 Comparison of Maximum Offsite Airborne Concentrations with 10 CFR 20 Limits (Braidwood) 11.3-33 11.3-8 Atmospheric Dilution Factors Used in Determining Offsite Doses (Braidwood) 11.3-34 11.3-9 Braidwood - Expected Individual Doses from Gaseous Effluents 11.3-35 11.3-10 Exhaust Stack Airflow Tabulation 11.3-38 11.4-1 Solid Waste Mana gement Syste m Equipment and Storage Design Capacities (Byron) 11.4-52 11.4-2 Expected and Design Basis Annual Volumes of (Units 1 and 2)
Solid Waste Management System Output (Byron) 11.4-56 11.4-3 Plant Interfac es with Solid Radwaste System (Byron) 11.4-57 11.4-1 Solid Waste Mana gement Syste m Equipment and Storage Design Capacities (Braidwood) 11.4-64
B/B-UFSAR 11.0-viii REVISION 6 - DECEMBER 1996 LIST OF TABL ES (Cont'd)
NUMBER TITLE PAGE 11.4-2 Expected and Des ign Basis Annual Volumes of (Units 1 and 2)
Solid Waste Management System Output (Braidwood) 11.4-68 11.4-3 Plant Interface with Solid Radwaste System (Braidwood) 11.4-69 11.5-1 Airborne Process and Effluent Monitors 11.5-17 11.5-2 Process Liquid Monitors 11.5-26 11.5-3 Radiological Analysis Summary of Liquid Process Samples 11.5-30 11.5-4 Radiological Analysis Summary of Gaseous Process Samples 11.5-31 11.5-5 Radiological Analysis Summary of Liquid Effluent Samples 11.5-32 11.5-6 Radiological Analysis Summary of Gaseous Effluent Samples 11.5-33
B/B-UFSAR 11.0-ix REVISION 9 - DECEMBER 2002 CHAPTER 11.0 -
RADIOACTIVE WASTE MANAGEMENT LIST OF FIGURES NUMBER TITLE 11.2-1 through 11.2-41 Deleted 11.3-1 Deleted 11.3-2 Gaseous Wast e Processing System Flow Diagram 11.4-1 Radwaste Disposal Sy stem Flow Diagram (Byron) 11.4-1 Radwaste Disposal Syst em Flow Diagram (Braidwood) 11.4-2 Deleted 11.4-3 Deleted 11.4-4 Deleted
B/B-UFSAR 11.0-x REVISION 9 - DECEMBER 2002 CHAPTER 11.0 -
RADIOACTIVE WASTE MANAGEMENT DRAWINGS CITED IN THIS CHAPTER*
- The listed drawings are included as "General Re ferences" only; i.e., refer to the drawings to obtain ad ditional detail or to obtain background info rmation. These drawin gs are not part of the UFSAR. They are controlled by the Control led Documents Program. DRAWING* SUBJECT M-9 General Arrangement Floor Pl an At EL. 383'-0" Units 1 and 2 M-12 General Arrangement Radwaste
/Service Building Units 1 & 2 M-24-1 to -20 General Arrangements , Radiation Shield ing Units 1 &
2 M-48-1 Diagram of Waste Disposal 30,000 Gallon Release Tank Units 1 & 2 M-48-2 Diagram of Waste Disposal Steam Generator Blowdown Units 1 & 2 M-48-3A, -3B Diagram of Waste Disposal Blowdown Mixed Bed Demineralizer Units 1 & 2 M-48-4A, -4B Diagram of Waste Disposal Blowdown Monitor Tanks Units 1 & 2 M-48-4C Diagram of Waste Dis posal Vacuum Pumps M-48-5A, -5B Diagram of Waste Disposal Steam Generator Blowdown Units 1 & 2 M-48-6A, -6B Diagram of Waste Disposal Auxiliary Building Floor Drains Units 1 & 2 M-48-7 Diagram of Waste Disposal (Liquid) Chemical &
Demineralizer Waste Regen.
Drains Units 1 & 2 M-48-8 Diagram of Waste Disposal Laundry Waste Drains Units 1 & 2 M-48-9 Diagram of Waste Disposal Radwaste Evaporator Units 1 & 2 M-48-10 Diagram of Waste Disposal Radwaste Evaporator "OA" Units 1 & 2 M-48-11, -12 Diagram of Waste Disposal Radwaste Evaporator "OB" Units 1 & 2 M-48-13 Diagram of Waste Disposal Radwaste Evaporator Units 1 & 2 M-48-14 Diagram of Waste Disposal Radwaste Evaporator "OC" Units 1 & 2
B/B-UFSAR 11.0-xi REVISION 9 - DECEMBER 2002 DRAWINGS CITED IN TH IS CHAPTER* (Cont'd)
DRAWING* SUBJECT M-48-15 Diagram of Waste Disposal Radwaste Monitor Tanks Units 1 & 2 M-48-16 Diagram of Waste Disposal Turbine Building Floor Drains Units 1 & 2 M-48-17 Diagram of Waste Disposal Auxiliary Building Equipment Drains Units 1 & 2 M-48-18 Diagram of Waste Disposal Resin Removal Units 1 & 2 M-48-19 Diagram of Miscellaneous Sum ps & Pumps Units 1 & 2 M-48-20A,
-20B Diagram of Waste Disposal Blowdown Mixed Bed Demineralizer Units 1 & 2 M-48-21A, -21B, -21C Diagram of Waste Disposal Radwaste Mixed Bed Demineralizer Units 1 & 2 M-48-22 Diagram of Waste Disposal Turbine Building Equipment Drains Units 1 & 2 M-48-23 Diagram of Radioactive W aste Reprocessing &
Disposal Units 1 & 2 M-48-24 Diagram of Turbine Build ing Waste Oil Collection System Units 1 & 2 M-48-25 Diagram of Auxiliary Bui lding Waste Oil Collection System Units 1 & 2 M-48-28 Diagram of Auxiliary Building Leak D etection Sumps Units 1 & 2 M-48-29 Diagram of Auxil iary Building Chromated Drain Collection System Units 1 & 2 M-48-30 Diagram of Miscellaneous Sump & Pumps Units 1 & 2 M-38-31 Blowdown Radwaste Mixed Bed Demineralizer Regeneration Skid Units 1 & 2 M-48-32 Diagram of Cement Filling Station Units 1 & 2 M-48-37 Diagram of Turbi ne Bldg Equipm ent/Floor Drain Coalescers Units 1 & 2 M-48-38 Diagram of Radwaste Evap orator Ammonia Stripper "A" Unit 1 & 2 M-48-39 Diagram of Radwaste Evap orator Ammonia Stripper "B" Unit 1 & 2 M-48-40 Diagram of Radwaste Evap orator Ammonia Stripper "C" Unit 1 & 2 M-48A Composite Diagram of L iquid Radwaste Treatment Processing Units 1 & 2
B/B-UFSAR 11.0-xii REVISION 9 - DECEMBER 2002 DRAWINGS CITED IN TH IS CHAPTER* (Cont'd)
DRAWING* SUBJECT M-64 Diagram of Chemical & Vo lume Control
& Boron Thermal Regenera tion Unit 1 M-64A Diagram of Chemical & Vo lume Control
& Boron Thermal Regenera tion Unit 1 M-69 Diagram of Radioacti ve Waste Gas Sys tem Units 1 & 2
B/B-UFSAR 11.3-11 TABLE 11.3-1 GASEOUS WASTE PROCESSING SYSTEM COMPONENT DATA
WASTE GAS COMPRESSORS
Number 2
Type Liquid seal rotary type
Design Flow rate, N 2 40 (at 140° F, 2 psig), cfm Design pressure, psig 150
Design temperature, °F 180 Normal operating pressure, psig Suction 0.5 - 2.0 Discharge 0 - 110 Normal operating temperature, °F 60 - 140 GAS DECAY TANKS
Number 6
Volume, each, ft 3 600 Design pressure, psig 150
Design temperature, °F 180 Normal operating pressure, psig 0 - 125 Normal operating temperature, °F 50 - 140 Material of construction Carbon steel
B/B-UFSAR
11.3-12
REVISION 11 - DECEMBER 2006 TABLE 11.3-2 GASEOUS WASTE PROCESSING SYSTEM INSTRUMENTATION DESIGN PARAMETERS
DESIGN DESIGN INSTRUMENT LOCATION OF PRESSURE TEMP. ALARM CONTROL LOCATION OF NUMBER PRIMARY SENSOR (psig)
(°F) RANGE SETPOINT SETPOINT READOUT TEMPERATURE INSTRUMENTATION TI-1029 Seal water, compressor No. 1 150 300 30-300°F NA NA At Waste Gas (Dial Thermometer) Compressor
TI-1034 Seal water, compressor No. 2 150 300 30-300°F NA NA At Waste Gas (Dial Thermometer) Compressor
PRESSURE INSTRUMENTATION PICA-1025 Vent header Hi, 2.5 psig 3.0 psig WPS panel 100 180 0 - 5 psig (BR) (BR) 2.0 psig (BY) 2.0 psig (BY)
Lo 2.0 psig (BR) 0.5 psig (BY)
PC-1028 (AB) Compressor No. 1 150 180 0 - 150 psig Hi, 100 psig Lo, 30 psig 100 psig WPS panel PC-1035 (AB) Compressor No. 2 150 180 0 - 150 psig Hi, 100 psig Lo, 30 psig 100 psig WPS panel PICA-1036 Waste gas decay tank No. 1 150 180 0 - 150 psig Hi, 95 psig 95 psig WPS panel (BR) 100 psig (BY)
_____________________
F - Flow R - Radiation P - Pressure I - Indication L - Level C - Control T - Temperature A - Alarm
B/B-UFSAR
11.3-13 REVI SION 10 - DECEMBER 2004 TABLE 11.3-2 (Cont'd)
DESIGN DESIGN INSTRUMENT LOCATION OF PRESSURE TEMP. ALARM CONTROL LOCATION OF NUMBER PRIMARY SENSOR (psig)
(°F) RANGE SETPOINT SETPOINT READOUT PICA-1037 Waste gas decay tank No. 2 150 180 0 - 150 psig Hi, 95 psig 95 psig WPS panel (BR)
PICA-1038 Waste gas decay tank No. 3 150 180 0 - 150 psig Hi, 95 psig 95 psig WPS panel (BR) 100 psig (BY)
PICA-1039 Waste gas decay tank No. 4 150 180 0 - 150 psig Hi, 95 psig 95 psig WPS panel (BR) 100 psig (BY)
PI-1047 Nitrogen header 150 180 0 - 25 psig NA NA Local
PICA-1052 Waste gas decay tank No. 5 150 180 0 - 150 psig Hi, 95 psig 95 psig WPS panel (BR) 100 psig (BY)
PICA-1053 Waste gas decay tank No. 6 150 180 0 - 150 psig Hi, 95 psig 95 psig WPS panel (BR) 100 psig (BY)
PIA-1065 Hydrogen header 150 180 50 - 150 psig Hi, 130 psig NA WPS panel Lo, 90 psig PIA-1066 Nitrogen header 150 180 50 - 150 psig Hi, 110 psig NA WPS panel Lo, 90 psig
B/B-UFSAR
11
.3-14 REVISION 13 - DECEMBER 2010 TABLE 11.3-2 (Cont'd)
DESIGN DESIGN INSTRUMENT LOCATION OF PRESSURE TEMP. ALARM CONTROL LOCATION OF NUMBER PRIMARY SENSOR (psig)
(°F) RANGE SETPOINT SETPOINT READOUT LEVEL INSTRUMENTATION LICA-1030 Waste gas compressor No. 1 150 180 0 - 28 in. Hi, 15 in. (BR) Inches: WPS panel 21 in. (BY) 15, 13 Lo, 1 in. 10, 7, 1 (BR) 21, 15 7, 4, 1 (BY)
LICA-1032 Waste gas compressor No. 2 150 180 0 - 28 in. Hi, 15 in. (BR) Inches: WPS panel 21 in. (BY) 15, 13 Lo, 1 in. 10, 7, 1 (BR) 21, 15 7, 4, 1 (BY)
RADIATION INSTRUMENTATION RICA-014 Plant vent See Section 11.5
GAS ANALYZER Located in separate cubicle in Aux. Bldg.
O/AIT-GW8003 (Byron)/
O/AT-GW8003 (Braidwood) Oxygen 300 212 0-19.99% 2% (Byron) none Local O/AR-GW8003 (Braidwood) Oxygen 300 212 0-5% 2% none Local O/AIT-GW004 Oxygen 300 212 0-5% 2% none Local O/AIT-GW8000 (Byron)/
O/AT-GW8000 (Braidwood) Hydrogen 25 130 0-100% - none Local O/AR-GW8000 (Braidwood) Hydrogen 25 130 0-100% - none Local
B/B-UFSAR
11.3-15
REVISION 3 - DECEMBER 1991 TABLE 11.3-3 PROCESS PARAMETERS AND REALISTIC, OPERATION BASIS ACTIVITIES IN GASEOUS WASTE SYSTEM(1) (CONCENTRATIONS IN
µC/cm 3)
POS NO.(2) LOCATION PRESSURE (psig) TEMP. (°F) FLOW RATE (cm 3/day) KR83M(4) KR85M(4) KR85 KR87 KR88 1 Unit 1 RCDT Vent 1.5 170 max. 1.14E+6 6.6E-04 1.9E-06 1.0E-04 1.0E-05 1.6E-05 2 Unit 2 RCDT Vent 1.5 170 max. 1.14E+6 6.6E-04 1.9E-06 1.0E-04 1.0E-05 1.6E-05 3 Sampling System VCT Vent Unit 1 1.5 115 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 4 Sampling System VCT Vent Unit 2 1.5 115 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 5 Vent Boron Recycle Holdup Tank - - 2.18E+7 1.2E-05 2.9E-08 9.5E-05 4.7E-07 3.2E-07 Vent 6 Gas Analyzer 3.5 VAR 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 7 Waste Disposal System SRST Vent - - 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 8 BRS Evaporator Unit 1 Vent (3) 1.5 155 3.82E+5 8.1E-04 1.9E-06 1.9E-02 3.2E-05 2.1E-05 9 BRS Evaporator Unit 2 Vent (3) 1.5 155 3.82E+5 8.1E-04 1.9E-06 1.9E-02 3.2E-05 2.1E-05 10 CVCS VCT Vent Unit 1 1.5 115 0 1.0E-01 8.8E-01 1.6E+01 2.2E-01 1.3E+00 11 CVCS VCT Vent Unit 2 1.5 115 0 1.0E-01 8.8E-01 1.6E+01 2.2E-01 1.3E+00 12 Combination of Normal Letdown 1.5 VAR 2.48E+7 4.5E-04 1.1E-06 7.8E-03 1.5E-05 1.2E-05 GWPS (5) 13 Compressor Recirculation Line 1.5 140 0 4.5E-04 1.1E-06 7.8E-03 1.5E-05 1.2E-05
B/B-UFSAR
11.3-16 REVISI ON 1 - DECEMBER 1989 TABLE 11.3-3 (Cont'd)
POS NO.(2) LOCATION PRESSURE (psig) TEMP. (°F) FLOW RATE (cm 3/day) KR89 XE131M(4) XE144M(4) XE133 XE135M(4) 14 Compressor Inlet 1.5 VAR 2.48E+7 4.5E-04 1.1E-06 7.8E-03 1.5E-05 1.2E-05 15 Compressor Inlet 0.5 VAR 2.48E+7 4.5E-04 1.1E-06 7.8E-03 1.5E-05 1.2E-05 16 Downstream of Compressor 110 max. 140 2.48E+7 4.5E-04 1.1E-06 7.8E-03 1.5E-05 1.2E-05 17 Compressor Outlet to Gas Decay - - 0 4.5E-04 1.1E-06 7.8E-03 1.5E-05 1.2E-05 Tanks 18 Inlet to Filling Gas Decay Tanks 110 max. 140 2.48E+7 4.5E-04 1.1E-06 7.8E-03 1.5E-05 1.2E-05 19 Line to Gas Decay Tank Header 110 AMB VAR 5.4E-06 3.0E-09 7.8E-03 1.2E-06 2.0E-07 20 Discharge Line 20 AMB VAR 0.0E+00 0.0E+00 7.7E-03 0.0E+00 0.0E+00 21 Discharge Line 1 AMB VAR 0.0E+00 0.0E+00 7.7E-03 0.0E+00 0.0E+00 22 Gas Analyzer 3.5 VAR 0 0.0E+00 0.0E+00 0.0E-00 0.0E+00 0.0E+00 23 From Gas Decay Tanks to Compressor 110 AMB 1.64E+8 5.4E-06 3.0E-09 7.8E-03 1.2E-06 2.0E-07 Inlet 24 From Gas Decay Tanks to BRS 3 AMB 1.64E+8 5.4E-06 3.0E-09 7.8E-03 1.2E-06 2.0E-07 HTs(6)
___________________
AMB - Ambient VAR - Variable
B/B-UFSAR 11.3-17 TABLE 11.3-3 (Cont'd)
POS NO.(2) LOCATION PRESSURE (psig) TEMP. (°F) FLOW RATE (cm 3/day) KR89 XE131M(4) XE133M(4) XE133 XE135M(4) 1 Unit 1 RCDT Vent 1.5 170 max. 1.14E+6 6.4E-06 2.1E-05 1.7E+00 3.1E+01 1.1E-01 2 Unit 2 RCDT Vent 1.5 170 max. 1.14E+6 6.4E-06 2.1E-05 1.7E+00 3.1E+01 1.1E-01 3 Sampling System VCT Vent Unit 1 1.5 115 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 4 Sampling System VCT Vent Unit 2 1.5 115 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 5 Vent Boron Recycle Holdup Tank - - 2.18E+7 9.4E-08 9.9E-06 2.5E-02 8.6E+00 1.6E-03 Vent 6 Gas Analyzer - - 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 7 Waste Disposal System SRST Vent - - 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 8 BRS Evaporator Unit 1 Vent (3) 1.5 155 3.82E+5 6.2E-06 1.1E-03 1.7E+00 7.3+02 1.1E-01 9 BRS Evaporator Unit 2 Vent (3) 1.5 155 3.82E+5 6.2E-06 1.1E-03 1.7E+00 7.3+02 1.1E-01 10 CVCS VCT Vent Unit 1 1.5 115 0 1.0E-03 1.6E+00 2.4E+00 2.2E+02 1.2E-02 11 CVCS VCT Vent Unit 2 1.5 115 0 1.0E-03 1.6E+00 2.4E+00 2.2E+02 1.2E-02 12 Combination of Normal Letdown 1.5 VAR 2.48E+7 3.7E-06 4.6E-04 9.9E-01 3.1E+02 6.4E-02 GWPS (5) 13 Compressor Recirculation Line 1.5 140 0 3.7E-06 4.6E-04 9.9E-01 3.1E+02 6.4E-02 14 Compressor Inlet 1.5 VAR 2.48E+7 3.7E-06 4.6E-04 9.9E-01 3.1E+02 6.4E-02
B/B-UFSAR
11.3-18 REVISI ON 1 - DECEMBER 1989 TABLE 11.3-3 (Cont'd)
POS NO.(2) LOCATION PRESSURE (psig) TEMP. (°F) FLOW RATE (cm 3/day) KR89 XE131M(4) XE133M(4) XE133 XE135M(4) 15 Compressor Inlet 0.5 VAR 2.48E+7 3.7E-06 4.6E-04 9.9E-01 3.1E+02 6.4E-02 16 Downstream of Compressor 110 max. 140 2.48E+7 3.7E-06 4.6E-04 9.9E-01 3.1E+02 6.4E-02 17 Compressor Outlet to Gas Decay - - 0 3.7E-06 4.6E-04 9.9E-01 3.1E+02 6.4E-02 Tank 18 Inlet to Filling Gas Decay 110 max. 140 2.48E+7 3.7E-06 4.6E-04 9.9E-01 3.1E+02 6.4E-02 Tanks 19 Line to Gas Decay Tank Header 110 AMB VAR 1.2E-09 3.5E-04 1.6E-03 1.8E-02 1.0E-04 20 Discharge Line 20 AMB VAR 0.0E+00 1.0E-05 0.0E+00 6.4E-02 0.0E+00 21 Discharge Line 1 AMB VAR 0.0E+00 1.0E-05 0.0E+00 6.4E-02 0.0E+00 22 Gas Analyzer 2 AMB 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 23 From Gas Decay Tank To 110 AMB 1.64E+8 1.2E-09 3.5E-04 1.6E-03 1.8E-02 1.0E-04 Compressor Inlet 24 From Gas Decay Tanks to BRS 3 AMB 1.64E+8 1.2E-09 3.5E-04 1.6E-03 1.8E-02 1.0E-04 Hts(6)
___________________ AMB - Ambient VAR - Variable
B/B-UFSAR 11.3-19 TABLE 11.3-3 (Cont'd)
POS NO.(2) LOCATION PRESSURE (psig) TEMP. (°F) FLOW RATE (cm 3/day) XE135 XE137 XE138 I130 I131 1 Unit 1 RCDT Vent 1.5 170 max. 1.14E+6 4.9E+01 1.4E-05 4.1E-01 1.1E-05 1.8E-06 2 Unit 1 RCDT Vent 1.5 170 max. 1.14E+6 4.9E+01 1.4E-05 4.1E-01 1.1E-05 1.8E-06 3 Sampling System VCT Vent Unit 1 1.5 115 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 4 Sampling System VCT Vent Unit 2 1.5 115 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 5 Boron Recycle Holdup Tank Vent - - 2.18E+7 1.8E+00 2.1E-07 6.2E-03 3.9E-08 5.7E-08 6 Gas Analyzer - - 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 7 Waste Disposal System SRST Vent - - 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 8 BRS Evaporator Unit 1 Vent (3) 1.5 1.5 3.82E+5 1.2E+02 1.4E-05 4.1E-01 0.0E+00 0.0E+00 9 BRS Evaporator Unit 2 Vent (3) 1.5 1.5 3.82E+5 1.2E+02 1.4E-05 4.1E-01 0.0E+00 0.0E+00 10 CVCS VCT Vent Unit 1 1.5 115 0 3.0E+00 2.2E-03 3.7E-02 0.0E+00 0.0E+00 11 CVCS VCT Vent Unit 2 1.5 115 0 3.0E+00 2.2E-03 3.7E-02 0.0E+00 0.0E+00 12 Combination of Normal Letdown to 1.5 VAR 2.48E+7 5.9E+01 8.1E-06 2.4E-01 2.0E-06 3.4E-07 GWPS (5) 13 Compressor Recirculation Line 1.5 140 0 5.9E+01 8.1E-06 2.4E-01 2.0E-06 3.4E-07 14 Compressor Inlet 1.5 VAR 2.48E+7 5.9E+01 8.1E-06 2.4E-01 2.0E-06 3.4E-07 15 Compressor Inlet 0.5 VAR 2.48E+7 5.9E+01 8.1E-06 2.4E-01 2.0E-06 3.4E-07
B/B-UFSAR
11.3-20
REVISION 1 - DECEMBER 1989 TABLE 11.3-3 (Cont'd)
POS NO.(2) LOCATION PRESSURE (psig) TEMP. (°F) FLOW RATE (cm 3/day) XE135 XE137 XE138 I130 I131 16 Downstream of Compressor 110 max. 140 2.48E+7 5.9E+01 8.1E-06 2.4E-01 2.0E-06 3.4E-07 17 Compressor Outlet to Gas Decay Tanks - - 0 5.9E+01 8.1E-06 2.4E-01 2.0E-06 3.4E-07 18 Inlet to Filling Gas Decay Tanks 110 max. 140 2.48E+7 5.9E+01 8.1E-06 2.4E-01 2.0E-06 3.4E-07 19 Line to Gas Decay Tank Header 110 AMB VAR 3.4E+00 3.3E-09 4.3E-04 1.5E-07 2.3E-07 20 Discharge Line 20 AMB VAR 0.0E+00 0.0E+00 0.0E+00 0.0E+00 1.3E-09 21 Discharge Line 1 AMB VAR 0.0E+00 0.0E+00 0.0E+00 0.0E+00 1.3E-09 22 Gas Analyzer 2 AMB 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 0.0E+00 23 From Gas Decay Tanks To Compressor 110 AMB 1.64E+8 3.4E+00 3.3E-09 4.3E-04 1.5E-07 2.3E-07 Inlet 24 From Gas Decay Tanks To BRS HTs(6) 3 AMB 1.64E+8 3.4E+00 3.3E-09 4.3E-04 1.5E-07 2.3E-07
___________________
AMB - Ambient VAR - Variable
B/B-UFSAR 11.3-21 TABLE 11.3-3 (Cont'd)
POS NO.(2) LOCATION PRESSURE (psig) TEMP. (°F) FLOW RATE (cm 3/day) I132 I133 I134 I135 1 Unit 1 RCDT Vent 1.5 170 max. 1.14E+6 1.6E-07 2.3E-06 4.4E-08 8.4E-07 2 Unit 1 RCDT Vent 1.5 170 max. 1.14E+6 1.6E-07 2.3E-06 4.4E-08 8.4E-07 3 Sampling System VCT Vent Unit 1 1.5 115 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 4 Sampling System VCT Vent Unit 2 1.5 115 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 5 Boron Recycle Holdup Tank Vent - - 2.18E+7 2.9E-10 1.2E-08 7.4E-11 2.1E-09 6 Gas Analyzer - - 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 7 Waste Disposal System SRST Vent - - 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 8 BRS Evaporator Unit 1 Vent (3) 1.5 155 3.82E+5 0.0E+00 0.0E+00 0.0E+00 0.0E+00 9 BRS Evaporator Unit 2 Vent (3) 1.5 155 3.82E+5 0.0E+00 0.0E+00 0.0E+00 0.0E+00 10 CVCS VCT Vent Unit 1 1.5 155 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 11 CVCS VCT Vent Unit 2 1.5 155 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 12 Combination of Normal Letdown to GWPS (5) 1.5 VAR 2.48E+7 2.8E-08 4.1E-07 7.6E-09 1.5E-07 13 Compressor Recirculation Line 1.5 140 0 2.8E-08 4.1E-07 7.6E-09 1.5E-07 14 Compressor Inlet 1.5 VAR 2.48E+7 2.8E-08 4.1E-07 7.6E-09 1.5E-07 15 Compressor Inlet 0.5 VAR 2.48E+7 2.8E-08 4.1E-07 7.6E-09 1.5E-07
B/B-UFSAR
11.3-22 REVISI ON 1 - DECEMBER 1989 TABLE 11.3-3 (Cont'd)
POS NO.(2) LOCATION PRESSURE (psig) TEMP. (°F) FLOW RATE (cm 3/day) I132 I133 I134 I135 16 Downstream of Compressor 110 max. 140 2.48E+7 2.8E-08 4.1E-07 7.6E-09 1.5E-07 17 Compressor Outlet to Gas Decay Tanks - - 0 2.8E-08 4.1E-07 7.6E-09 1.5E-07 18 Inlet to Filling Gas Decay Tanks 110 max. 140 2.48E+7 2.8E-08 4.1E-07 7.6E-09 1.5E-07 19 Line to Gas Decay Tank Header 110 AMB VAR 3.9E-10 5.4E-08 4.1E-11 6.1E-09 20 Discharge Line 20 AMB VAR 0.0E+00 0.0E+00 0.0E+00 0.0E+00 21 Discharge Line 1 AMB VAR 0.0E+00 0.0E+00 0.0E+00 0.0E+00 22 Gas Analyzer 2 AMB 0 0.0E+00 0.0E+00 0.0E+00 0.0E+00 23 From Gas Decay Tanks To Compressor Inlet 110 AMB 1.64E+8 3.9E-10 5.4E-08 4.1-11 6.1E-09 24 From Gas Decay Tanks To BRS HTs (6) 3 AMB 1.64E+8 3.9E-10 5.4E-08 4.1-11 6.1E-09
___________________
AMB - Ambient VAR - Variable
B/B-UFSAR 11.3-23 TABLE 11.3-3 (Cont'd)
NOTES:
- 1. This is a synthe sis of information from operating reactors.
- 2. These position numbe rs correspond to positions marked on Figure 11.3-2.
- 3. Boron Recycle System (BRS).
- 4. Metastable (M).
- 5. Gaseous Waste Pr ocessing System (GWPS).
- 6. Holdup Tank (HT)
B/B-UFSAR
11.3-24 REVISION 3
- DECEMBER 1991 TABLE 11.3-4 ASSUMPTIONS USED IN CALC ULATING EXPECTED SYSTEM ACTIVITIES A. EXPECTED SYSTEM ACTIVITY
- 1. The major inputs to the gas sy stem during normal operation are vents on the Boron Recyc le System (BRS) holdup tanks (HUT), reactor coolant drain tanks (RCDT) and BRS evaporators. Inputs from the gas analyzer sampling system and CVCS volume control tank are assumed to be negligible.
- 2. Reactor coolant gase ous activities are b ased on Regulatory Guide 1.112 as modified to reflect Byr on/Braidwood plant parameters.
- 3. Twenty-five percent of dissolved radioga ses in the reactor coolant entering the RCDTs a nd HUTs leave solution and enter the vapor space.
- 4. Radioactive decay was assumed while the BRS HUTs, RCDTs and gas decay tanks were filling.
No additional decay was assumed in the evaporator.
- 5. The BRS HUT is assum ed to be filled to 80% capacity before processing by the BRS evaporat or. The RCDTs are assumed to be filled to 280 ga llons before draining.
- 6. Values for liquid flow rates to the ta nks were based on estimates of ann ual average flows:
BRS HUT flow 1.0 gpm (0.5 gpm per unit) RCDT flow 300 gpd (per each unit)
BRS Evaporator flow 1.0 gpm (0.5 gpm/evaporator - from BRS HUTs)
- 7. The plant capacity factor is 0.8.
- 8. The iodine parti tion coefficient in the RCDTs and BRS HUTs was: liquid in cc/Ci vapor in cc/Ci 10 X 5.7 3µµ (Based on Regulatory Guide 1.112).
- 9. The hydrogen con centration in the primary coolant was assumed 35 cc/kg.
B/B-UFSAR
11.3-2 5 REVISION 3 -
DECEMBER 1991 TABLE 11.3-4 (Cont'd)
B. ANNUAL RELEASES The following additional assumptions were us ed in calculating expected annual releases:
- 1. One refueling per ye ar per unit was assu med, with complete degassing of reactor coolant and also transfer of noble gases and iodines present in the volume control tank vapor space at shutdown to the gaseous waste s ystem. This gaseous activity is rele ased after 60 days decay for this analysis only.
- 2. Kr-85 release to the environment is based on an entry rate of 0.15 Ci/MWt-yr Kr
-85 into the primary coolant. It was assumed that all Kr-85 entering the cool ant is eventually released to the environment.
- 3. From the calcula tion of system activities, t he activity in a single gas decay tank was determined a fter 60 days decay. It was assumed that one tank was released every 60 days for purposes of this analysis only.
B/B-UFSAR 11.3-26 TABLE 11.3-5 TYPICAL GASEOUS RELEASES FROM OPERATING REACTORS
NOBLE GASES (10 3 Ci) 73 74 75 R. E. Ginna 0.576 0.78 1.81 Connecticut Yankee 0.032 0.008 1.81
San Onofre 11.0 1.78 1.07 Surry 1 & 2 0.87 54.4 9.47
H. B. Robinson 2 3.1 0.27 0.707
Point Beach 1 & 2 5.75 9.71 32.1
IODINES (Ci) 73 74 75 R. E. Ginna 0.0006 0.0004 0.0037 Connecticut Yankee 0.0013 0.0001 0.0009 San Onofre 0.42 0.0002 0.0046
Surry 1 & 2 0.042 0.071 0.0456 H. B. Robinson 2 0.296 0.012 0.0115 Point Beach 1 & 2 0.011 0.098 0.0188
B/B-UFSAR
11.3-27 R
EVISION 1 - DECEMBER 1989 TABLE 11.3-6 EXPECTED ANNUAL AVERAGE RELEASE OF AIRBORNE RADIONUCLIDES
- , ** GASEOUS RELEASE RATE - CURIES PER YEAR PRIMARY SECONDARY BLOWDOWN AIR COOLANT COOLANT GAS STRIPPING BUILDING VENTILATION VENT EJECTOR NUCLIDE (µCi/g) (µCi/g) SHUTDOWN CONTINUOUS REACTOR AUXILIARY TURBINE OFF-GAS EXHAUST TOTAL KR 83M 2.265-02 6.255-09 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 KR 85M 1.184-01 3.337-08 0.0 0.0 0.0 3.0+00 0.0 0.0 2.0+00 5.0+00
KR 85 1.051-01 2.944-08 5.1+01 5.7+02 7.4+01 2.0+00 0.0 0.0 1.0+00 7.0+02
KR 87 6.474-02 1.726-08 0.0 0.0 0.0 1.0+00 0.0 0.0 0.0 1.0+00
KR 88 2.156-01 5.928-08 0.0 0.0 0.0 5.0+00 0.0 0.0 3.0+00 8.0+00
KR 89 5.399-03 1.512-09 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
XE131M 1.035-01 2.917-08 4.0+00 1.5+01 1.7+01 2.0+00 0.0 0.0 1.0+00 3.9+01
XE133M 2.293-01 6.461-08 0.0 0.0 7.0+00 5.0+00 0.0 0.0 3.0+00 1.5+01
XE133 1.804+01 5.010-06 2.4+01 4.7+01 1.3+03 3.8+02 0.0 0.0 2.4+02 2.0+03 XE135M 1.404-02 3.887-09 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
XE135 3.755-01 1.041-07 0.0 0.0 2.0+00 8.0+00 0.0 0.0 5.0+00 1.5+01
- 0.0 appearing in the table indicates release is less than 1.0 Ci/yr for noble gas, 0.0001 Ci/yr for I.
- For one unit. KEY: 4.5-03 = 4.5 x 10
-3 B/B-UFSAR
11.3-28 R
EVISION 1 - DECEMBER 1989 TABLE 11.3-6 (Cont'd)
GASEOUS RELEASE RATE - CURIES PER YEAR PRIMARY SECONDARY BLOWDOWN AIR COOLANT COOLANT GAS STRIPPING BUILDING VENTILATION VENT EJECTOR NUCLIDE (µCi/g) (µCi/g) SHUTDOWN CONTINUOUS REACTOR AUXILIARY TURBINE OFF-GAS EXHAUST TOTAL XE137 9.719-03 2.700-09 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
XE138 4.751-02 1.296-08 0.0 0.0 0.0 1.0+00 0.0 0.0 0.0 1.0+00 TOTAL NOBLE GASES 2.8+03 I 131 2.795-01 4.215-05 0.0 0.0 1.7-03 4.4-02 2.3-03 0.0 2.8-03 5.1-02
I 133 3.986-01 3.831-05 0.0 0.0 7.7-04 6.3-02 2.1-03 0.0 4.0-03 7.0-02
TRITIUM GASEOUS RELEASE 1000 CURIES/YR
B/B-UFSAR 11.3-29 TABLE 11.3-6 (Cont'd)
AIRBORNE PARTICULATE RELEASE RATE - CURIES PER YEAR 1
WASTE GAS BUILDING VENTILATION NUCLIDE SYSTEM REACTOR AUXILIARY TOTAL MN 54 4.5-03 6.1-06 1.8-04 4.7-03 FE 59 1.5-03 2.1-06 6.0-05 1.6-03 CO 58 1.5-02 2.1-05 6.0-04 1.6-02 CO 60 7.0-03 9.5-06 2.7-04 7.3-03 SR 89 3.3-04 4.7-07 1.3-05 3.4-04 SR 90 6.0-05 8.4-08 2.4-06 6.2-05 CS134 4.5-03 6.1-06 1.8-04 4.7-03 CS137 7.5-03 1.1-05 3.0-04 7.8-03
- In addition to these re leases, 25 Ci/yr of argo n-41 are released from the containment and 8 Ci/yr of carbon-14 are released from the w aste gas processing sy stem. This table was developed taking into ac count both releases from normal oper ations and also operational occurrences.
KEY: 4.5-03 = 4.5 x 10
-3 B/B-UFSAR
11.3-3 0 REVISION 6 -
DECEMBER 1996 TABLE 11.3-6 (Cont'd)
VOLUME REDUCTION SYSTEM*
RELEASE RATE (Ci/yr)
Noble Gases: Xe 131m 5.1-01 Xe 133m 1.2+00 Xe 133 2.1+01
Halogens: I 131 2.8-03 I 132 3.7-03 I 133 2.1-03 Tritium: H 3 2.6+01
Particulates: Cr 51 5.3-08 Fe 55 7.0-07 Co 58 6.0-07 Co 60 9.2-08 Ni 63 7.0-07 Y 91 1.5-09 Mo 99 3.5-07 Tc 99m 2.1-09 Te 132 1.5-07 Cs 134 1.1-05 Cs 136 1.9-07 Cs 137 7.4-07
KEY: 5.1-01 = 5.1x10
-1
- The original est imate included r elease data for the volume reduction system. This system is no longer used.
BYRON-UFSAR 11.3-31 REVISION 5 - DECEMBER 1994 TABLE 11.3-7 COMPARISON OF MAXIMU M OFFSITE AIRBORNE CONCENTRATIONS WITH 10 CFR 20 LIMITS MAXIMUM SITE ANNUAL RELEASE BOUNDARY
- FROM ONE UNIT CONCENTRATION CONCENTRATION ISOTOPE (Ci/yr)
(µCi/ml) (µCi/ml) H 3 1.0+03 3.5-11 2.0-07 C 14 8.0+00 2.8-13 1.0-07 Ar 41 2.5+01 8.8-13 4.0-08 Kr 85m 5.0+00 1.8-13 1.0-07 Kr 85 7.0+02 2.5-11 3.0-07 Kr 87 1.0+00 3.5-14 2.0-08 Kr 88 8.0+00 2.8-13 2.0-08 Xe 131m 4.0+01 1.4-12 4.0-07 Xe 133m 1.6+01 5.6-13 3.0-07 Xe 133 2.0+03 7.0-11 3.0-07 Xe 135 1.5+01 5.3-13 1.0-07 Xe 138 1.0+00 3.5-14 3.0-08 I 131 5.4-02 1.9-15 1.0-10 I 132 3.7-03 1.3-16 3.0-09 I 133 7.2-02 2.5-15 4.0-10 Cr 51 5.3-08 1.9-21 8.0-08 Mn 54 4.7-03 1.7-16 1.0-09 Fe 55 7.0-07 2.5-20 3.0-08 Fe 59 1.6-03 5.6-17 2.0-09 Co 58 1.6-02 5.6-16 2.0-09 Co 60 7.3-03 2.6-16 3.0-10 Ni 63 7.0-07 2.5-20 2.0-09 Sr 89 3.4-04 1.2-17 3.0-10 Sr 90 6.2-05 2.2-18 3.0-11 Y 91 1.5-09 5.3-23 1.0-09 Mo 99 3.5-07 1.2-20 7.0-09 Tc 99m 2.1-09 7.4-23 5.0-07 Te 132 1.5-07 5.3-21 4.0-09 Cs 134 4.7-03 1.7-16 4.0-10 Cs 136 1.9-07 6.7-21 6.0-09 Cs 137 7.8-03 2.7-16 5.0-10
- 0.26 mi E /Q = 1.11 x 10
-6 sec/m 3 ** Limits used are those that were in effect at the time of the analysis.
KEY: 3.5 - 11 = 3.5 x 10-11 BYRON-UFSAR 11.3-32 REVISION 1 - DECEMBER 1989 TABLE 11.3-8 ATMOSPHERIC DILUTION FACTORS USED IN DETERMINING OFFSITE DOSES
/Q 2 D/Q* LOCATION (sec/m
- 3) (l/m 2) Nearest site boundary (0.26 mi E) 1.11 - 06 7.86 - 09
Nearest residence (0.30 mi ESE) 7.61 - 07 6.39 - 09 Nearest garden (0.60 mi SW) 1.43 - 07 1.68 - 09
Nearest meat animal (0.60 mi SSE) 2.53 - 07 1.75 - 09 Nearest milk cow (1.50 NE) 1.09 - 07 8.71 - 10
- Calculated using the methodology of NRC Regu latory Guide 1.111, Revision 1, July 1977.
KEY: l.ll - 06 = 1.11 x 10
-6
BYRON-UFSAR 11.3-33 TABLE 11.3-9 BYRON-EXPECTED INDIVID UAL DOSES FROM G ASEOUS EFFLUENTS DOSE RATE (mrem/yr)
LOCATION PATHWAY TOTAL BODY SKIN THYROID BONE LIVER LUNG GI-LLI Nearest Residence Plume 0.023 0.073 (0.3 mi ESE) Ground Deposition 0.057 0.067 Inhalation Adult 0.030 0.048 0.004 0.030 0.032 0.030 Teen 0.031 0.053 0.00 5 0.031 0.033 0.031 Child 0.027 0.054 0.007 0.028 0.029 0.027 Infant 0.016 0.040 0.005 0.016 0.017 0.016 Nearest Garden Leafy Vegetables (0.6 mi SW) Adult 0.006 0.028 0.002 0.00 6 0.006 0.006 Teen 0.004 0.023 0.00 2 0.004 0.004 0.004 Child 0.005 0.033 0.004 0.005 0.005 0.005 Stored Vegetables Adult 0.083 0.081 0.033 0.084 0.079 0.081 Teen 0.103 0.102 0.05 7 0.108 0.100 0.101 Child 0.169 0.171 0.138 0.180 0.167 0.167 Nearest Meat Meat Animal Adult 0.019 0.023 0.016 0.01 9 0.019 0.019 (0.6 mi SSE) Teen 0.013 0.016 0.014 0.013 0.013 0.013 Child 0.017 0.021 0.025 0.017 0.016 0.016 Nearest Milk Cow Milk (1.5 mi NE) Adult 0.027 0.102 0.012 0.02 7 0.025 0.025 Teen 0.037 0.164 0.02 4 0.040 0.036 0.035 Child 0.062 0.321 0.059 0.069 0.061 0.060 Infant 0.099 0.730 0.113 0.115 0.099 0.097 BRAIDWOOD-UFSAR 11.3-34 REVISION 5 - DECEMBER 1994 TABLE 11.3-7 COMPARISON OF MAXIMU M OFFSITE AIRBORNE CONCENTRATIONS WITH 10 CFR 20 LIMITS
- 0.30 mi NW /Q = 8.10 x 10
-7 sec/m 3 ** Limits used are those that were in effect at the time of the analysis.
KEY: 2.6 - 11 = 2.6 x 10-11 MAXIMUM SITE ANNUAL RELEASE BOUNDARY 3 10 CFR 20
- FROM ONE UNIT CONCENTRATION CONCENTRATION ISOTOPE (Ci/yr)
(µCi/ml) (µCi/ml) H 3 1.0+03 2.6-11 2.0-07 C 14 8.0+00 2.0-13 1.0-07 Ar 41 2.5+01 6.4-13 4.0-08 Kr 85m 5.0+00 1.3-13 1.0-07 Kr 85 7.0+02 1.8-11 3.0-07 Kr 87 1.0+00 2.6-14 2.0-08 Kr 88 8.0+00 2.1-13 2.0-08 Xe 131m 4.0+01 1.0-12 4.0-07 Xe 133m 1.6+01 4.1-13 3.0-07 Xe 133 2.0+03 5.1-11 3.0-07 Xe 135 1.5+01 3.9-13 1.0-07 Xe 138 1.0+00 2.6-14 3.0-08 I 131 5.4-02 1.4-15 1.0-10 I 132 3.7-03 9.5-17 3.0-09 I 133 7.2-02 1.8-15 4.0-10 Cr 51 5.3-08 1.4-21 8.0-08 Mn 54 4.7-03 1.2-16 1.0-09 Fe 55 7.0-07 1.8-20 3.0-08 Fe 59 1.6-03 4.1-17 2.0-09 Co 58 1.6-02 4.1-16 2.0-09 Co 60 7.3-03 1.9-16 3.0-10 Ni 63 7.0-07 1.8-20 2.0-09 Sr 89 3.4-04 8.7-18 3.0-10 Sr 90 6.2-05 1.6-18 3.0-11 Y 91 1.5-09 3.9-23 1.0-09 Mo 99 3.5-07 9.0-21 7.0-09 Tc 99m 2.1-09 5.4-23 5.0-07 Te 132 1.5-07 3.9-21 4.0-09 Cs 134 4.7-03 1.2-16 4.0-10 Cs 136 1.9-07 4.9-21 6.0-09 Cs 137 7.8-032.0-165.0-10 BRAIDWOOD-UFSAR 11.3-35 TABLE 11.3-8
ATMOSPHERIC DILUTION FACTORS USED IN DETERMINING OFFSITE DOSES
/Q 4 D/Q* LOCATION (sec/m
- 3) (l/m 2) Nearest site boundary (0.30 mi NW) 8.10 - 07 4.36 - 09
Nearest residence (0.30 mi NW) 8.10 - 07 4.36 - 09 Nearest garden (0.30 mi NW) 8.10 - 07 4.36 - 09
Nearest meat animal (1.70 mi NW) 7.73 - 08 4.49 - 10
Nearest milk cow (1.7 mi WSW) 7.79 - 07 3.70 - 10 Nearest milk goat (4.1 mi E) 3.43 - 08 1.49 - 10
- Calculated using the methodology of NRC Regu latory Guide 1.111, Revision 1, July 1977.
KEY: 8.10 - 07 = 8.10 x 10-7 BRAIDWOOD-UFSAR
11.3-36
REVISION 3 -
DECEMBER 1991 TABLE 11.3-9
BRAIDWOOD-EXPECTED I NDIVIDUAL DOSES FROM GASEOUS EFFLUENTS
DOSE RATE (mrem/yr)
LOCATION PATHWAY TOTAL BODY SKIN THYROID BONE LIVER LUNG GI-LLI Nearest Residence Plume 0.023 0.074 (0.3 mi NW) Ground Deposition 0.039 0.046 Inhalation Adult 0.035 0.054 0.004 0.035 0.037 0.035 Teen 0.036 0.059 0.00 5 0.036 0.038 0.036 Child 0.032 0.060 0.007 0.032 0.034 0.032 Infant 0.019 0.044 0.005 0.019 0.020 0.019 Nearest Garden Leafy Vegetables (0.3 mi NW) Adult 0.035 0.090 0.012 0.03 5 0.034 0.034 Teen 0.025 0.072 0.01 2 0.025 0.024 0.024 Child 0.031 0.102 0.022 0.031 0.030 0.030 Stored Vegetables Adult 0.498 0.491 0.173 0.500 0.488 0.491 Teen 0.622 0.619 0.29 8 0.634 0.614 0.616 Child 1.025 1.029 0.727 1.053 1.019 1.018 Nearest Meat Meat Animal Adult 0.006 0.007 0.005 0.00 6 0.006 0.006 (1.7 mi NW) Teen 0.004 0.005 0.004 0.004 0.004 0.004 Child 0.005 0.006 0.008 0.005 0.005 0.005
BRAIDWOOD-UFSAR 11.3-37 TABLE 11.3-9 (Cont'd)
DOSE RATE (mrem/yr)
LOCATION PATHWAY TOTAL BODY SKIN THYROID BONE LIVER LUNG GI-LLI Nearest Milk Cow Milk (1.7 mi WSW) Adult 0.020 0.051 0.008 0.02 0 0.019 0.019 Teen 0.028 0.081 0.01 6 0.029 0.027 0.027 Child 0.047 0.155 0.040 0.050 0.047 0.046 Infant 0.075 0.339 0.077 0.082 0.075 0.075 Nearest Milk Goat Milk (4.1 mi E) Adult 0.018 0.032 0.004 0.01 8 0.017 0.017 Teen 0.024 0.049 0.00 8 0.026 0.023 0.023 Child 0.039 0.091 0.020 0.043 0.039 0.038 Infant 0.061 0.188 0.038 0.068 0.061 0.060
B/B-UFSAR 11.3-38 REVISION 2 - DECEMBER 1990 TABLE 11.3-10 EXHAUST STACK AI RFLOW TABULATION CASE 1 CASE 2 REFUELING EXCEPTNORMAL PLANT MINI-FLOW (cfm) OPERATION (cfm) UNIT 1 Auxiliary Building Exhaust 135,980 135,980 Laboratory System Exhaust 14,430 (Byron) 14,430 (Byron) 13,030 13,030 (Braidwood) (Braidwood)
Off Gas System Steam Jet Air Ejector 0 32 Gland Steam Condenser Exhaust0 1,400 Containment Purge System Mini-Purge Exhaust (3000 CFM)0 0
Main-Purge Exhaust 43,900 0 194,310 (Byron) 151,842 (Byron) 192,910 150,442 (Braidwood) (Braidwood) UNIT 2 Auxiliary Building Exhaust 135,980 135,980 Auxiliary Building Filtered Vents 1,000 1,000 Solid Radwaste Area Exhaust 8,630 8,630 Off Gas System Steam Jet Air Ejector 0 32 Gland Steam Condenser Exhaust 0 1,400 Containment Purge System Mini-Purge Exhaust (3000 CFM)0 0
Main-Purge Exhaust 43,900 0 189,510 147,042
BYRON-UFSAR
11.4-52 REVISION 7 - DECEMBER 1998 TABLE 11.4-1 SOLID WASTE MANAGEME NT SYSTEM EQUIPMENT AND STORAGE DESI GN CAPACITIES
PROCESSING EQUIPMENT QUANTITYDESIGN CAPACITY MATERIALS Decanting tank 2 500 gallons 304L SS Decanting pump 2 18 gpm 304L SS
Metering pump 4 15 gpm 304L SS
Cement storage tank 1 1000 ft 3 CS Drum processing unit 2 1 Drum 304L SS Packaging container (drum) - 55 gallons CS Packaging container (liner)- Up to 200 ft 3 CS or Polyethylene
Dry waste compactor 1 1 Drum CS
Traveling bridge crane 1 1 9.3 tons CS Fixed bridge crane 1 2 1.0 ton CS Drum transfer car 2 2 2 drums CS Startup heater 1 395 scfm 304SS/
347SS
Air heater 1 320 scfm 304SS/
316L-SS Gas heater 1 786 scfm 304SS/
Fluid bed dryer air blower 1 317 scfm CS
Dry waste processor air blower 1 300 scfm CS
BYRON-UFSAR
11.4-53 TABLE 11.4-1 (Cont'd)
PROCESSING EQUIPMENT QUANTITYDESIGN CAPACITY MATERIALS Waste feed filter 1 30 gpm 316L-SS FBD inlet air filter 1 320 scfm CS
DWP inlet air filter 1 300 scfm CS
Gas filter assembly 2 466 scfm CS
Recirculating gas filter 1 320 scfm CS
Caustic tank 1 1000 gal 304SS Decon tank 1 650 gal 304SS Contaminated oil tank 1 150 gal CS
Bed storage and transfer hopper 2 2900 lb 304SS
Trash hopper 2 1500 lb CS/Fe
Waste liquor storage tank 2 3500 gal 316L-SS Fluid bed dryer 1 0.41 gpm 347SS/ Inconel 625
Dry waste processor 1 83 lb/hr 347SS
Trash conveyor 1 --- Rubber/CS
Trash elevator 1 20 lb/min CS
Waste feed pump 1 120 gph 316L-SS Waste recirc. pump 2 500 gpm 316L-SS Decon. pump 1 50 gpm 304SS
Dryer feed pump 1 30 gph 316L-SS Condensate pump 1 22 gpm 316SS
Contaminated oil pump 1 14 gpm CS Scrubber preconcentrator recirc. pump 1 20 gpm 316L-SS
Caustic additive pump 2 15 gpm 304SS
BYRON-UFSAR
11.4-54 TABLE 11.4-1 (Cont'd)
PROCESSING EQUIPMENT QUANTITY DESIGN CAPACITY MATERIALS Scrubber preconcentrator 1 16.8 gpm 316L-SS/ Inconel 625 Secondary scrubber 1 1142 scfm 316L-SS Condenser 1 22 gpm 316SS Metal detector 1 1 Trash Bag Al,Cu Volume reduction system 1 911 scfm 347SS gas/solids separator Trash shredder 1 20 lb/min Fe/CS/CrMo Steel Polymer storage tank 2 3000 gal 304L Promoter additive 1 6 gal 304 storage tank Isolation hopper 1 7.5 ft 3 316L-SS Storage hopper 1 80 ft 3 304L-SS Drum processing 1 1 drum 304L enclosure Flame arrester 2 --- --- Volume reduction system 1 250 scfm 304L solidification system gas/solid separator Volume reduction product 1 250 scfm SA285 Gr. C blower Polymer circulating pump 1 15gpm/7.5gpm 316SS Promoter metering pump 1 10oz/min 420SS Roller conveyor 1 30 fpm CS Polymer filter 1 65 gpm 304SS Polymer station vent filter1 75 scfm 304SS Volume reduction solidi- 1 180 scfm 304L fication system product blower filter
BYRON-UFSAR
11.4-55 REVISION 7 - DECEMBER 1998 TABLE 11.4-1 (Cont'd)
STORAGE AREA NUMBER OF STORAGE AREAS DESIGN CAPACITY PER STORAGE AREA Low level 1 500 drums or 30 containers
Intermediate level 1 640 drums or 30 containers
Dry compacted waste 1 70 drums
Dry uncompacted waste 1 90 ft 3
Empty drum or container 2 100 drums or 6 containers (total)
NOTES 1. Overhead Crane Operating Speeds High-Speed Low-Speed
Bridge 125 fpm 2.5 fpm
Trolley 125 fpm 2.5 fpm
Drum Grab Hoist 30 fpm 7.5 fpm
- 2. Drum Transfer Car Operating Speeds High-Speed Low-Speed
100 fpm 10 fpm
BYRON-UFSAR
11.4-56
REVISION 7 - DECEMBER 1998 TABLE 11.4-2 EXPECTED AND DESIGN BASIS ANNUAL VOLUMES OF (UNITS 1 AND 2)
SOLID WASTE MANAGEME NT SYSTEM OUTPUT*
Solid waste processed by the solid r adwaste management system and quant ities of processed was te requiring onsite storage or offsi te disposal EXPECTED NUMBER OF DESIGN NUMBER OF TYPE OF WASTE VOLUMES CONTAINERS VOLUME CONTAINERS Deep Bed Resin 1,600 ft 3 2,393 drums 1,600 ft 3 2,393 drums or 10 liners or 10 liners Disposable Filter Elements 75 ft 3 190 drums 75 ft 3 190 drums or 2 liners or 2 liners Sludges and Liquids*** 16,850 ft 3 4,580 drums 18,690 ft 3 5,140 drums Dry Active Waste 36,220 ft 3 580** drums 36,220 ft 3 1,160** drums 73 boxes 73 boxes Total 54,745 ft 3 7,743 drums, 56,585 ft 3 8,883 drums, 73 boxes 73 boxes or 12 liners, or 12 liners, 5,350 drums 6,490 drums and 73 boxes and 73 boxes
___________________
- The values given are approxi mate. The actual data a re available in the effluent release reports, which a re prepared in accorda nce with the ODCM. ** Not solidified. *** Sludges and liqu ids are normally processed in the liquid radwaste system.
BYRON-UFSAR
11.4-57
REVISION 6 - DECEMBER 1996 TABLE 11.4-3
PLANT INTERFACES WITH SOLID RADWASTE SYSTEM ESTIMATED ESTIMATED GROSS INTERFACE NUMBER LINE* LINE EXPECTED TEMPERATURE EXPECTED ESTIMATED RADIOISOTOPE AND DESCRIPTION NUMBER SIZE PRESSURE (°F) FLOW RATE BATCH SIZE CONCENTRATION**** 1. Spent Resin OWXX9A 1-1/2 in. 50 psig 90 120 gpm up to 400 gal 370 Ci/cc
- 2. Evaporator Concentratesf OWX143BA 1-1/2 in. 35 psig 130-90 15 gpm 22.5-36.5 gal** 0.05 Ci/cc
- 3. Flush and Decontamination OWX146BA 1-1/2 in. 52 psig 110 50 gpm 25 gal 0.16 Ci/cc
- 4. Volume Reduction System***
- a. Evaporator concentrates OVR80A 1-1/2 in. 35 psig 190 30 gpm 3500 gal 0.05 Ci/cc
- b. Waste oil OVR69A 2 in. 25 psig 150 50 gpm 140 gal low
- Typical line numbers, for Unit B line numbers the last letter is B.
- Directly to the drum from a recirculation loop via a metering pump.
- Byron does not operate the volume reduction system.
- Based on Table 11.1-11.
f Evaporator concentrates are normally processed in the liquid radwaste system.
BYRON-UFSAR
11.4-58 TABLE 11.4-3 (Cont'd)
ESTIMATED ESTIMATED GROSS INTERFACE NUMBER LINE* LINE EXPECTED TEMPERATURE EXPECTED ESTIMATED RADIOISOTOPE AND DESCRIPTION NUMBER SIZE PRESSURE (°F) FLOW RATE BATCH SIZE CONCENTRATION**** c. Pump seals/dilution OPW60A 2 in. 50 psig 120 75 gpm continuous Primary water intermittent
- d. Decon water supply OPMK7A 2 in. 135 psig 100 100 gpm 600 gal Primary
- e. Cooling water supply OWSJ4A 4 in. 140 psig 110 156 gpm continuous 0.0
- f. Cooling water return OWSJ6A 3 in. 140 psig 124 156 gpm continuous 0.0
- g. Service air supply 2SA67A 1-1/2 in. 115/90 psig 120 78 scfm continuous 0.0
- h. Filtered exhaust OVR084B 6 in. 2 in. H 2O 175 477 scfm continuous 5.6 x 10
-4 Ci/cc
- i. Drains OWF69A 3 in. 50 psig 150 50 gpm intermittent 2.7 x 10
-2 Ci/cc j. Decon water return OVR123A 2 in. 50 psig 180 50 gpm 150 gal 0.05 Ci/cc
- k. Filter backwash inlet OVR81A 3/4 in. 150 psig 250 50 gpm 50 gal Primary water
- l. Filter backwash outlet OVR13A 3/4 in. 150 psig 200 50 gpm 50 gal 0.5 Ci/cc
- m. Instrument air OVA210A 1 in. 115 psig 150 82 scfm continuous 0.0
- n. Bed storage hopper fill OVR47A 6 in. ambient ambient gravity 50 lb 0.0
- o. Dry active water - - ambient ambient 20 ft 3/min 7.5 ft 3 Low
BYRON-UFSAR
11.4-59 RE VISION 6 - DECEMBER 1996 TABLE 11.4-3 (Cont'd)
ESTIMATED ESTIMATED GROSS INTERFACE NUMBER LINE* LINE EXPECTED TEMPERATURE EXPECTED ESTIMATED RADIOISOTOPE AND DESCRIPTION NUMBER SIZE PRESSURE (°F) FLOW RATE BATCH SIZE CONCENTRATION**** 9. Volume Reduction System***
Production Solidification System
- a. Cooling water supply OWO120A 1-1/2 in. 100 psig 100 10 gpm intermittent 0.0
- b. Cooling water return OWO128A 1-1/2 in. 100 psig 100 10 gpm intermittent 0.0
- c. Instrument air (polymer) OIA117A 1 in. 115 psig 120 5 scfm intermittent 0.0
- d. Instrument air OVR257A 1/2 in. 115 psig 120 58 scfm intermittent 0.0 (equipment)
- e. Instrument air OVR255A 1 in. 115 psig 120 58 scfm continuous 0.0 (equipment) f. Instrument air OVR256A 3/4 in. 115 psig 120 58 scfm intermittent 0.0 (storage hopper)
- g. Instrument air (blower) OVR258A 1 in. 115 psig 120 60 scfm intermittent 0.0
- h. Drain (drum processing) OVR169A 3 in. 4 psig 180 20 gpm intermittent Low
- i. Drain (storage hopper) OVR173A 2 in. 4 psig 180 15 gpm intermittent 8.4 x 10
-2 Ci/cc
- j. Drain (surge hopper) OVR181A 1-1/2 in. 4 psig 180 5 gpm intermittent 8.4 x 10
-2 Ci/cc
- k. Polymer filling ------- 2 in. -1 in. H 2O ambient 10 scfm continuous 0.0 station vent
- l. Blower discharge OVR180A 2-1/2 in. 0.5 psig 120 60 scfm intermittent Low
B/B-UFSAR
11.4-60 through 11.4-63 REVISION 6 - DECEMBER 1996
Pages 11.4-60 through 11.4-63 have been deleted intentionally.
BRAIDWOOD-UFSAR
11.4-64 REVISION 12 - DECEMBER 2008 TABLE 11.4-1 SOLID WASTE MANAGEME NT SYSTEM EQUIPMENT AND STORAGE DESI GN CAPACITIES
PROCESSING EQUIPMENT QUANTITY DESIGN CAPACITY MATERIALS Packaging container - up to 200 ft 3 CS or (liner) polyethylene Packaging container (drum) - 55 gal CS Traveling bridge crane 1 1 9.3 tons CS Fixed bridge crane 1 2 1.0 ton CS Drum transfer car 2 2 2 drums CS Cartridge filter transfer vehicle 3 1 1 drum CS
NOTE: Processing equipment for the volume reduction and radwaste solidification systems has been intentio nally deleted from this table. Braidwo od station does not intend to use this equipment.
BRAIDWOOD-UFSAR
11.4-65 REVISION 9 - DECEMBER 2002 TABLE 11.4-1 (Cont'd)
Page 11.4-65 has bee n deleted intentionally.
BRAIDWOOD-UFSAR
11.4-66 REVISION 9 - DECEMBER 2002 TABLE 11.4-1 (Cont'd)
Page 11.4-66 has bee n deleted intentionally.
BRAIDWOOD-UFSAR
11.4-67 REVISION 7 - DECEMBER 1998 TABLE 11.4-1 (Cont'd)
NUMBER OF DESIGN CAPACITY STORAGE AREA STORAGE AREAS PER STORAGE AREA Low level 1 500 drums or 30 containers
Intermediate level 1 640 drums or 30 containers
Dry compacted waste 1 70 drums
Dry uncompacted waste 1 90 ft 3 Empty drum or container 2 100 drums or 6 containers (total)
NOTES 1. Overhead Crane Operating Speeds High-Speed Low-Speed Bridge 125 fpm 2.5 fpm Trolley 125 fpm 2.5 fpm
Drum Grab Hoist 30 fpm 7.5 fpm
- 2. Drum Transfer Car Operating Speeds High-Speed Low-Speed 100 fpm 10 fpm
- 3. Cartridge Filter Transfer Vehicle Operating Speeds Variable
0 fpm to 250 fpm
BRAIDWOOD-UFSAR
11.4-68
REVISION 7 - DECEMBER 1998 TABLE 11.4-2 EXPECTED AND DESIGN BASIS ANNUAL VOLUMES OF (UNITS 1 AND 2)
SOLID WASTE MANAGEME NT SYSTEM OUTPUT*
Solid waste processed by the solid r adwaste management system and quant ities of processed waste requiring onsite storage or of fsite disposal
EXPECTED NUMBER OF DESIGN NUMBER OF TYPE OF WASTE VOLUMES CONTAINERS VOLUME CONTAINERS Deep Bed Resin 1,600 ft 3 10 liners 1,600 ft 3 10 liners Disposable Filter Elements 75 ft 3 2 liners 75 ft 3 2 liners Sludges and Liquids*** 16,850 ft 3 141 liners 18,690 ft 3 156 liners Dry Active Waste 36,220 ft 3 580 drums** 36,220 ft 3 1,160 drums** 73 boxes 73 boxes Total 54,745 ft 3 153 liners 56,585 ft 3 168 liners 580 drums 1,160 drums 73 boxes 73 boxes
___________________
- The values given are approxi mate. The actual data are available in the effluent release reports, which are p repared in accordance with the ODCM. ** Not solidified.
- Sludges and liquids are no rmally processed in the liquid radwaste system.
BRAIDWOOD-UFSAR
11.4-69
REVISION 6 - DECEMBER 1996 TABLE 11.4-3
PLANT INTERFACE WITH SOLID RADWASTE SYSTEM
ESTIMATED ESTIMATED GROSS INTERFACE NUMBER LINE* LINE EXPECTED TEMPERATURE EXPECTED ESTIMATED RADIOISOTOPE AND DESCRIPTION NUMBER SIZE PRESSURE (°F) FLOW RATE BATCH SIZE CONCENTRATION** 1. Spent Resin OWX425A 1-1/2 in. 75 psig 90 40 gpm up to 845 gal 1500 Ci/cc
- 2. Evaporator Concentrates*** OWXZ9D 1-1/2 in. 109 psig 130-190 45 gpm 100 gal 0.05 Ci/cc
- 3. Resin Flush and Decontamination OWX137A 2 in. 50 psig 120 50 gpm 115 gal 0.16 Ci/cc
- 4. Pump Seals
- a. Evaporator concentrates OWX530AA 1/2 in. 5 psig ambient .25 gpm intermittent Low
- b. Spent resin OWX589CA 3/8 in. 90 psig 120 .25 gpm intermittent Primary water
- 5. Volume Reduction Systemf
- a. Waste oil OVR69A 2 in. 25 psig 150 50 gpm 140 gal low
- b. Pump seals/dilution water OWMK7A 2 in. 135 psig 100 75 gpm continuous 0.0 intermittent
- c. Decon water supply OWMK7A 2 in. 135 psig 100 100 gpm 600 gal 0.0
- Typical line numbers, for Unit B line numbers the last letter is B.
- Based on Table 11.1-11. *** Evaporator concentrates are normally processed in the liquid radwaste system. f Braidwood does not operate the volume reduction system.
BRAIDWOOD-UFSAR
11.4-70
REVISION 6 - DECEMBER 1996 TABLE 11.4-3 (Cont'd)
ESTIMATED ESTIMATED GROSS INTERFACE NUMBER LINE* LINE EXPECTED TEMPERATURE EXPECTED ESTIMATED RADIOISOTOPE AND DESCRIPTION NUMBER SIZE PRESSURE (°F) FLOW RATE BATCH SIZE CONCENTRATION** d. Cooling water supply OWSJ4A 4 in. 140 psig 110 156 gpm continuous 0.0
- e. Cooling water supply OWSJ6A 3 in. 140 psig 124 156 gpm continuous 0.0
- f. Filtered exhaust OVR084B 4 in. 2 in. H 2O 175 477 scfm continuous 5.6x10
-4 Ci/cc
- g. Drains OWF69A 3 in. 50 psig 150 50 gpm intermittent 2.7x10
-2 Ci/cc
- h. Decon water supply OVR123A 2 in. 50 psig 180 50 gpm 150 gal 0.05 Ci/cc
- i. Filter backwash inlet OVR81A 3/4 in. 150 psig 250 50 gpm 50 gal Primary water
- j. Filter backwash outlet OVR13A 3/4 in. 150 psig 200 50 gpm 50 gal 0.5 Ci/cc
- k. Instrument air OVR210A 1 in. 115 psig 150 82 scfm continuous 0.0 l. Bed storage hopper fill OVR47A 6 in. ambient ambient gravity 50 lb Low
- m. Dry active waste - - ambient ambient 20 ft 3/min 7.5 ft 3 Low
- 6. Volume Reduction Systemf Production Solidification System
- a. Cooling water supply OWO348A 1-1/2 in. 100 psig 100 10 gpm intermittent 0.0
- b. Cooling water return OWO349A 1-1/2 in. 100 psig 100 10 gpm intermittent 0.0
- c. Instrument air (polymer) OIA116A 1 in. 115 psig 120 5 scfm intermittent 0.0
BRAIDWOOD-UFSAR
11.4-71 TABLE 11.4-3 (Cont'd)
ESTIMATED ESTIMATED GROSS INTERFACE NUMBER LINE* LINE EXPECTED TEMPERATURE EXPECTED ESTIMATED RADIOISOTOPE AND DESCRIPTION NUMBER SIZE PRESSURE (°F) FLOW RATE BATCH SIZE CONCENTRATION** d. Instrument air (drum processing) OVR257A 1/2 in. 115 psig 120 58 scfm intermittent 0.0
- e. Instrument air (equipment) OVR255A 1 in. 115 psig 120 58 scfm continuous 0.0
- f. Air bump (surge hopper) OVR307A 3/8 in. 40 psig 120 58 scfm intermittent 0.0
- g. Instrument air (storage hopper) OVR256A 3/4 in. 115 psig 120 58 scfm intermittent 0.0
- h. Air bump (storage hopper) OVR310A 3/8 in. 40 psig 120 58 scfm intermittent 0.0
- i. Instrument air (blower) OVR258A 1 in. 115 psig 120 60 scfm intermittent 0.0
- j. Drain (drum processing) OVR169A 3 in. 4 psig 180 20 gpm intermittent Low
- k. Drain (storage hopper) OVR173A 2 in. 4 psig 180 15 gpm intermittent 8.4x10
-2 Ci/cc
- l. Drain (surge hopper) OVR181A 1-1/2 in. 4 psig 180 5 gpm intermittent 8.4x10
-2 Ci/cc
- m. Polymer filling station vent ----- 2 in. -1 in. H 2O ambient 10 scfm continuous 0.0
- n. Blower discharge OVR180A 2-1/2 in. 0.5 psig 120 60 scfm intermittent Low
BRAIDWOOD-UFSAR
11.4-72 TABLE 11.4-3 (Cont'd)
ESTIMATED ESTIMATED GROSS INTERFACE NUMBER LINE* LINE EXPECTED TEMPERATURE EXPECTED ESTIMATED RADIOISOTOPE AND DESCRIPTION NUMBER SIZE PRESSURE (°F) FLOW RATE BATCH SIZE CONCENTRATION** 7. Vendor Supplied Mobile Radwaste System
- a. Instrument air O1A117A 3/4 in. 115 psig 120 50 scfm continuous 0.0
- b. Service air OSAR1A 3/4 in. 115 psig 120 50 scfm continuous 0.0
- c. Demineralized water OWMT2A 2 in. 135 psig 100 100 gpm intermittent 0.0
- d. Service water supply OWS59A 2 in. 140 psig 96 25 gpm continuous 0.0
- e. Service water return OWSX5A 2 in. 140 psig 96 25 gpm continuous 0.0
- f. Drain OWX439A 2 in. 100 psig 100 25 gpm continuous 0.16 Ci/cc
- g. Vent OVF075A 4 in. 3 psig 175 200 scfm continuous Low
BYRON/BRAIDWOOD STATIONS UPDATED FINAL SAFETY ANALYSIS REPORT FIGURE 11.3-2 GASEOUS WASTE PROCESSING SYSTEM FLOW DIAGRAM CARTRIDGE DRY ACTIVE FILTERS WASTES SLUDGES AND LIQUIDS LOW ACTMTY SPENT RESIN REVISION 6 DECEMBER 1996 HIGH ACTMTY SPENi RESIN HIGH ACTIVITY SPENT RESIN STORAGE TANK PACKAGE STORAGE AREA COMPACTOR PACKAGE SPENT RESIN.STORAGE TANK MOBILE t AUX.BLOC.MOBILE LINER STORAGE RADWASTE RADWASTE AREA , SYSTEM FLOOR DRAINS SYSTEM I UNER UNER STORAGE AREA TRUCK TRUCK TRUCK DISPOSAL SITE BRAIDWOOD STATION UPDATED FINAL SAFETY ANALYSIS REPORT FIGURE 11.4-1 RADWASTE DISPOSAL SYSTEM FLOW DIAGRAM CARTRIDGE DRY ACTIVE FILTERS WASTES SLUDGES AND LIQUIDS LOW ACTIVITY SPENT RESIN REVISION 6 DECEMBER 1996 HIGH ACTIVITY SPENT RESIN PACKAGE STORAGE AREA LINER TRUCK COMPACTOR PACKAGE STORAGE AREA TRUCK MOBILE RADWASTE SYSTEM LINER t AUX.BLOC.FLOOR ORAINS SPENT RESIN STORAGE TANK MOBILE RADWASTE SYSTEM LINER STORAGE AREA TRUCK DISPOSAL SITE BYRON STATION UPDATED FINAL SAFElY ANALYSIS REPORT FIGURE 11,4-1 RADWASTE DISPOSAL SYSTEM FLOW DIAGRAM