ML18360A476

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Attachment 8: 2017 Training Material on Diesel Generator Air Start Flow Plow
ML18360A476
Person / Time
Site: Clinton Constellation icon.png
Issue date: 12/14/2018
From:
Exelon Generation Co
To:
NRC/RGN-III, Office of Nuclear Reactor Regulation
Shared Package
ML18360A500 List:
References
RS-18-146
Download: ML18360A476 (162)


Text

ATTACHMENT 8 2017 Training Material on Diesel Generator Air Start Flow Path

Exelon Generation Course I Program: EO Continuing Lesson ID: N-CL-EOC-1701 2017 Cycle 1 Training (DG-DO,

Title:

ES-HD, FC, RW, VD, TREQs, LMS Component N-CL-NLO-RQ01 N Mods & LL)

Author: David Williams Revision / Date: 00 I 01/05/2017 Prerequisites: None Revision By: N/A Responsible Site: Clinton Power Station Est. Teach Time 10hr Approvals Qualified Nuclear Engineer (If NIA Date: NIA Applicable)

Training Supervision Dave Williams ISi Date: 0110612017 Review Program Owner Tim Windingland ISi Date: 0111012017 Approval

(

TQ-M-223-F045 Rev 004

© Copyright 2013 by Exelon Nuclear, All Rights Reserved. Permission for reproduction and use is reserved for Exelon Nuclear (Any other use or reproduction is expressly prohibited without the express permission of Exelon Nuclear.)

SRRS 3D.126/3D.111 Retain approved lessons for life of plant OR life of insurance Policy +1 yr for RP lessons. May be retained in-department for two years, then forwarded to RM

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation

. Lesson ID: N-CL-EOC-1701 Objectives Using normally available references, unless otherwise stated, and with 100% accuracy, in accordance with course reference materials and procedures, the trainee shall:

Objective Description ~ Slide(s}

233000.1.1 - STATE the purposes of the Fuel Pool Cooling & Cleanup System 20-22 including applicable design bases.

233000.1.2 - Describe the major flow paths for the following modes of the FC 23-29 system

.1 Normal Flow path

.2 RX vessel pool draindown

.3 RX vessel pool fill

.4 FC assist

.5 Alt Suppres~ion pool cooling 31 233000.1.6 - Given a Fuel Pool Cooling& Cleanup System Annunciator, DESCRIBE: 32

b. Any automatic actions 233000.1.7 - Given the Fuel Pool Cooling & Cleanup system, DESCRIBE the 33-36.

systems supporting and the nature of the support.

233000.1.15 - Given Fuel Pool Cooling & Cleanup System initial conditions, PREDICT how the system and/or plant parameters will respond to the manipulation of the following controls .

.2 Fuel Pool Cooling & Cleanup system Filter/Demin controls for Hold,

  • Filter, Backwash and Precoat
  • Lesson Title_: 2017 Cycle 1 Trainin*g (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Using the approved pro'cedure, DISCUSS: 1

~ Slide(s)

Task 331701.18 - Lower FC Surge Tank Level During System Operation 39 Task 331701.30 - Pump Casing Vent After Maintenance for the Fuel Pool Cooling 39 and Cleanup System

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Using normally available references, unless otherwise stated, and with 100% accuracy, in accordance with course reference materials and procedures, the trainee shall:

Objective Description ~ Slide(s) 264000.1.1 - STATE the purpose(s) of the DG/DO System including applicable 43-44 design bases.

264000.1.2 - Describe the major flow paths for the following modes of the DG/DO 45-47, 52-66 system

.1 Lube Oil Sys*

.2 Fuel Oil Sys

.3 Air Start Sys 264000.1.5 - Discuss the DG/DO system automatic functions/interlocks including 48-51 purpose, signals, set points, sensing points, when bypassed, how/when they are .

.6 Fuel Oil Storage Tank

.7 Fuel Oil Day Tank

.8 Fuel Oil Transfer Pump 264000.1.7 - Given the DG/DO system, DESCRIBE the systems supporting and 74-75 the nature of the support .

.1 DG Auto Starts

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL)

Lesson ID: N-CL-EOC-1701 Exelon Generation Objectives Using normally available references, unless otherwise stated, and with 100% accuracy, in accordance with course reference materials and procedures, the trainee shall:

Objective Description ~ Slide(s) 264000.1.11 - EVALUATE given key DG/DO System parameters, if needed 76-77(

DETERMINE a course of action to correct or mitigate the following -

abnormal condition(s):

.1 High Crankcase Pressure

.2 Overspeed

.3 Overcrank

~ .

.4 Low Oil Pressure

.5 High Water Temperature

.6 Reverse Power

.7 Loss of Excitation

.8 Overcurrent

.9 Generator Ground Fault

'.10 Differential Current

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Using the approved procedure, DISCUSS: .,

Task Description ~ Slide(s)

Task 350601.17 - Diesel Engine Lube Oil Addition or Removal 78 Task 350601.27 - Respond to DG 1A(18)[1 C] Auto Start 79 Task 350601.34D - Alternate Diesel Generator Start - Manual Override of Air 80 Start Solenoids

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Using normally available references, unless otherwise stated, and with 100% accuracy, in accordance with course reference materials and procedures, the trainee shall:

Objective Description ~ Slide(sj 233000.1.1 - STATE the purpose(s) of the DG ROOMS HVAC System including 83-84 applicable design bases.

233000.1.2 - Describe the major flow paths for the following modes of the DG 85-87 ROOMS HVAC system operation .

. 1 Normal Standby Mode

.2 Diesel Generator Operating Mode

.3 Purge Mode J

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & Lt)

Lesson ID: N-CL-EOC-1701 Exelon Generation Objectives Using the approved procedure, DISCUSS:

Task Description

~ Slide(s)

Task 340301.03 - Increased Cooling/PURGE Mode of the VD System 88-90 Task 340301.08 - Respond to a CO2 Initiation with respect to the VD System 91-92

Lesson

Title:

2017 Cycle 1 Training {DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Upon completio_n of this chapter, the student will be able to perform the following objectives at a minimum proficiency level of 80%, unless otherwise stated, on an oral or written exam:

Objective Description ~ Slide(s}

BC081r4_Controllers 4. State the purpose of a controller. 96 BC081r4_Controllers 5. Describe the theory of operation of the following types of controllers:

97-101

a. Two position
b. Proportional
c. Proportional-plus-reset (Pl)
d. Proportional-plus-reset-plus-rate BC081r4_Controllers 7. Describe the following characteristics of a flow control valve: 102
a. Linear
b. Quick opening
c. Equal percentage BC081r4_Contrqllers 9. State the function and describe the characteristics of valve positioners. 103-104 Treq 02422997-82 Discuss the operation of Bailey/NUS controllers at 1PA05J. 105

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL)

Lesson ID: N-CL-EOC-1701 Exelon Generation Objectives Upon completion of this chapte_r, the student will be able to perform the following objectives at a minimum proficiency level of 80%, unless otherwise stated, on an oral or written exam:

Objective Description ~ Slide(s) 239003.1.1 STATE the purpose(s) of the EXTRACTION STEAM, HEATER VENTS & DRAINS System including 107 applicable design bases.

239003.1.2 DESCRIBE the major flowpaths for the following modes of the EXTRACTION STEAM, HEATER VENTS & DRAINS System operation .

108-113

.1 Extraction Steam System while operating in the normal mode

.2 Extraction Steam System while operating in a specified abnormal mode

.3 Feedwater Heating Drain System while operating in the normal mode

.4 Feedwater Heating Drain System while operating in a specified abnormal mode 239003.1.3 DESCRIBE the function, operation, interlocks, trips, physical location, and power supplies of the following EXTRACTION STEAM, HEATER VENTS & DRAINS System components .

  • 114-119

.1 Feedwater Heaters

.2 Flash Tanks

.3 Drain Coolers

.4 Extraction Steam Isolation Valves

.5 Extraction Steam Check Valves

.6 Heater and Drain Cooler Normal Drain Valves

.7 Heater and Drain Cooler Emergency Drain Valves

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Upon completion of this chapter, the student will be able to perform the following objectives at a minimum proficiency level of 80%, unless otherwise stated, on an oral or written exam:

Objective Description ~ Slide(s) 239003.1.5 Discuss the EXTRACTION STEAM, HEATER VENTS & DRAINS system automatic 120 functions/interlocks including purpose, signals, set points, sensing points, when bypassed, how/when they are.

239003.1.11 EVALUATE given key EXTRACTION STEAM, HEATER VENTS & DRAINS System paramete~s. if needed DETERMINE a course of action to correct or mitigate the following abnor.mal condition(s): 121-122

.1 Low heater level on system performance

.2 Any heater reaching it's high level setpoint

.3

  • High heater level on system performance

.4 Any heater reaching it's high-high level setpoint

.5 Heater string isolation valve closure

.6 Loss of control power

.7 Effect on other heaters when heaters are removed from service/ returned to service Task310201.16 Respond to Feedwater Heater Abnormal Level 123-124 Task 310201.19 Preparing Feedwater Heater Level Control For Maintenance Or Trouble-Shooting Of A Normal Drain Valve Malfunction 125

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Using normally available references, unless otherwise stated, and with 100% accuracy, in accordance with course reference materials and procedures, the trainee shall:

Objective Description ~ Slide(s) 268013.1.1- STA TE the purposes of Spent Resin System 138.

268016.1.4- STATE the physical location and function of the following SOLID 127-130 RADWASTE .SLUDGE COLLECTION/DISPOSAL system controls, indicators, and/or sensors .

.9 Quantum Master Control Console

.10 Tank Level Instrumentation 145

. 268009.1.10- EXPLAIN the reasons for given RADWASATE DEMINERALIZERS System operating limits and precautions

.1 Reason for maintaining Resin Outlet Valve gagged shut during.

normal operations .

.2 Method of performing a Resin/Charcoal load .

.3 Method of performing a Resin unload .

.5 Loading charcoal prior to loading resin.

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Using the approved procedure, DISCUSS:

~ Slide(s)

Task 390901 ~02 - Spent Resin Tank-level readings, 17 Rese_tting a Locked Up 141-142 Quantum Master Controller ,

Task 390902.06 - Phase Separators Level Readings 131-137 Task 390903.02 - Waste Sludge Tanks level readings 137 Task 390904.03 - Concentrated Waste Tanks level readings 137 Task 390905.02 - FP/FD Sludge Tanks level readings 137 TREQ 02623308 Liquid RW Discharge Surveillance 146 TREQ 02623308 Resin Loading activities 143-144 TREQ 02623308 WX Tank Level Mod 139-141

Lesson

Title:

20i7 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL} Exelon Generation Lesson ID: N-CL-EOC-1701 Evaluation Methods and Passing Criteria For objectives: Written Examination with Score 2: 80%

For tasks: Satisfactory classroom participation, as decided by the instructor.

References

1. N-CL-OPS-233000, FC
2. N-CL-OPS-264000, DG-GO
3. N-CL-OPS-288006, VD
4. N-CL-OPS-239003, ES-HD
5. N-CL-OPS-268002, RW INTEGRATED LIQ COLLECTION AND PROCESSING
6. . N-CL-OPS-268008, RW FILTERS
7. N-CL-OPS-268009, RW DEMINERALIZERS
8. N-CL-OPS-268010, RW EVAPORATORS
9. N-CL-OPS-268011, RW WASTE SAMPLE
10. N-CL-OPS-268012, RW EXCESS WATER
11. N-CL-OPS-268013, RW SPENT RESIN .,*
12. N-CL-OPS-268014, RW CONCENTRATE WASTE
13. N-CL-OPS-268016, RW SOLID RW SLUDGE

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Evaluation Methods and Passing Criteria For objectives: Written Examination with Score 2: 80%

For tasks: Satisfactory classroom participation, as decided by the instructor.

References

14. CPS 3317.01, FUEL POOL COOLING AND CLEANUP (FC)
15. CPS 3317.02, FUEL POOL COOLING FILTER DEMINERALIZERS
16. CPS 5917, ALARM PANEL 5917 ANNUNCIATORS (OPL45J)
17. - CPS 3506.01, DIESEL GENERATOR AND SUPPORT SYSTEMS
18. CPS 3403.01, DIESEL GENERATOR HVAC (VD) .
19. CPS 3102.01, EXTRACTION STEAM-HTR VENT AND DRAINS
20. CPS 3906.01, OPERATING RW DEMINERLIZERS
21. CPS 3909.01, OPERATING SPENT RESIN SYSTEM
22. CPS 3909.02, OPERATING PHASE SEPARATORS
23. CPS 3909.03, OPERATING WASTE SLUDGE SYSTEM
24. CPS 3909.04, OPERATING CONCENTRATE WASTE SYSTEM
25. cps 3909.05, OPERATING FUEL POOL FILTER DEMIN SLUDGE SYSTEM
26. CPS 9911.50, LIQUID RADIOACTIVE DISCHARGE SURVEILLANCE
27. CY-AA-110-5002, BEAD RESIN USE AND CONTROL
28. BC081r4_CONTROLLERS (GF.ES)

Commitments Ensure the associated section is annotated in the right-hand column of the notes page NONE

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Instructor Materials

1. System procedures (as needed)
2. System lesson plan (as needed)
3. Classroom with overhead projection abilities Student Materials
1. lpads with Sharefile access

Focus Areas

  • Crew/ Dept Focus Areas PIIM HU Improvement Plan
  • -**-***---~

Your Role in Training Participation Questions Feedback Training Observations LASER Entries 18

    • ----------~

Ground Rules Return from breaks on time Pagers and phones on silent mode Practice good housekeeping E@

Phone calls, texting, and messages only on breaks, unless it is an emergency 19

20 Remove decay heat from the spent fuel assemblies Maintain pool water level Minimize fission product concentration in the water Maintain pool clarity for fuel handling Clean up the suppression pool Provide alternate suppression pool cooling 21

remove the decay heat remove radioactive contaminants

~ Minimize the radiation levels

~ Minimize release of radioisotopes 22

Flow Paths FROM UPPER POOLS A

HX FROM RHR

~

RHR FC FILTER PUMP SUCTION 023 B TO HX UPPER POOLS CASK SPE T 10RAGE FUB..

POOL POOL 23

CY ~ A Makeup GJB From CNMT Surge Upper Pools Tank Normal A

HX 035 014A l FCOlAA FCPump~-0 026A From RHR LC 024A To CNMT RHR - FC AHter Pump Upper Demineralizer B Suction 002 001 023 Pools HX

~

l FCO lAB FC Pump 8 0148 0268 To Equipment Drains 1FC127D 1FC133

_ _ _ _ _ __, i - - - t....t--1 Cask 5 orage 1FC127B To Fuel Building Fuel Pool Transfer Equipment Drain Pool Tank 1RE01T

< 1 ll FUEL POOL COOLING AND CLEANUP SYSTEM FLOW DIAGRAM

RX vessel Pool Draindown f tt tt .--------

~-* -----,

RHR _ _ _ ,

FROM 3111 3A TO CONDENSER FR OM CY FROM FC SUPPLY

~0-1CY010

~ TO 157 156 FC SURGE I

CNMT TANKS BOUNDARY CNMT BOUNDARY 136 FROM I RHR 38; 3fB I

I I I I 86B FILL LJNE t~ I I '

r r FC SYSTEM FLOW DIAGRAM CONTAINMENT POOLS 25

RX vessel Pool Draindown CY ~ A Makeup G.38 F rom CNMT U pper P ,o ols A

HX 0 14A l .FCOlAA F CPum p ~ - 0 ~

1 FC004A 026A From 0 16A RHR

.--------, 0 24A T o CNMT RHR - FC R.ilter Pump Upper Sucti on 002 001 023 B Pools HX t....-

176

~

l FCOlAB 177 B FC Pump B 026B To Surge Equ i pment Tank Dra i ns 1 FC127D Cask Spe n s orage 1 FC127B Fu e l Fu e l T o Fuel Bu il d i ng storage Pool Transfe r Equ i pment Dra in Pool T ank 1RE01 T Pool 1 ll FUEL POOL COOLING .AND CLEANUP SYSTEM FLO\N DIAGRAM

RX vessel Pool Draindown l 11 fl ll u TO CONDENSER FROM CY FROM FC SUPPLY

~ 0-1CY010

~ TO FC SURGE I

CNMT TANKS BOUNDARY A

Surge 136 Tank J 86B FI LL LINE B

Surge Tank Spen Fuel S orage 7 Pool M FLOW DIAGRAM CONTAINMENT POOLS

RX vessel Pool Fill t ft TO CONDENSER FROM FC SUPPLY

~ - TO - ~

157 156 FCSURGE CNMT TANKS BOUNDARY FRO RHR -_"'----'----- -,

3B; I I 1 oos RLLUNE I

FC Assist From CP T u119*' P.oois A

HX To C Upptf

~ ocn Pock

[IJII To

_M nt* *-

1fe127D RJEL POOL COOLING .N-10 CLEANUP SYSTEM FLO.IV DIAGRA 29

Interim Summary FROM UPPER POOLS 128 A HX FROM RHR

~

RHR FC FILTER PUMP SUCTION 023 B TO HX UPPER POOLS CASK SPE T TORAGE FUB..

PO OL POOL 30

CY ~ A Makeup {]J8 From CNMT Surge Upper Pools Tank 5917-48 Annunciator A HX 035 014A lFCOl AA FC Pump ~-0-----~~*---------

1FC004A 026A From 016A RHR .

LC To CNMT RHR - FC lter Pump Upper Demineralizer B Suction 002 001 Pools 016B HX

~

FCO l AB FC Pump B 0148 0268 B

To Surge Equipment Tank Drains 1FC127D 1FC127B To Fuel Building Fuel Equipment Drain Transfer Tank 1RE01T Pool 11 FUEL POOL COOLING AND CLEANUP SYSTEM FLOW DIAGRAM

Support Systems Component Cooling Water System (CCW)Shutdown Normal supply to FC HX and Pump Motor Coolers Service Water System (SX)

Backup supply to FC HX and Pump Motor Coolers Emergency Makeup to Spent Fuel Storage Pool Cycled Condensate System Makeup to FC Surge Tanks Fill supply to Upper Containment Pools F/D backwash and precoat Containment and RPV Isolation Control (CRVICS) System RPV Level 2 / High DW press isolation signals 32

Support Systems

-AC Electrical Distribution

-DC Electrical Distribution

-Leak Detection System CT, OW, AB, and FB Floor and Equipment Drain System

-Residual Heat Removal System

-Main Condenser

-Solid Radwaste Processing

-Process Sampling

-Service/Instrument Air System

-Fuel Building Ventilation

-Containment Ventilation/Drywell Purge

-Radwaste Building Ventilation 33

FD Train Manual Pushbuttons HOLD FILTER BACKWASH PRECOAT T ables Table l : Hold Pushbutton Actions and Effects Table :. Filter Pushbutton Actions and Effects Table 3:. Backwash Pushbutton Actions and Effects Table 4:: Pree oat Pushbutton Actions and Effects

Backwash Pushbutton Actions and Effects 1-1.1s.21 Initiating Event Action System Effects Press Backwash Backwash light comes on, PLC pushbu tton (PB-3) starts the process.

Backwash program sealed in.

058 closes FD inlet isolated from FC & SF systems.

068 opens Water begins to drain for FD vessel dome.

067 opens Service Air ad mitted to vessel dome 068 closes Vessel dome is pressurized.

062 closes, Hold Pump stops, 065 FD water & resin is fo rced out th ro ugh opens. main drain.

067 closes Serv ice Air is shut off.

065 closes Vessel drainage stops.

04 1, 063 & 066 open CY enters to fi ll FD & flush through overflow line.

069 opens Air enters fro m bottom of vessel to create froth ing action & dislodge resin from septa. (Air Scour) 069, 063, 066, & 04 1 close Vessel fill & scouring act ion stops.

067 opens Service Ai r pressurizes vessel dome.

065 opens FD vessel water and resi n is fo rced out through main drain.

067 closes Service Air to dome is shut off.

065 closes Vessel drainage stops.

PLC stops the process, Backwash light goes out, Shutdown light comes on.

35

Preco at Pu sh butt on Ac ti ons a nd Effe cts (. 1.1 5.2 (

l ni1 i:11 ing Evenl Acti on Sys tem Effec ts Press Precoat pushbutton (P B-4) PLC stans the process Shutdown light goes ou t, Backwash light comes on , and Precoat progra m is sealed in.

Backwash li ght goes out, Precoat light comes on , and Power Failure rel ay is reset (if necessary).

063, 066 and 04 1 o pen FD Vesse l fills with CY water.

PS-FC024 senses hi g h pressure 066 closes Vessel overflow stops.

in overnow lin e 066 opens Vessel overfl ow resum es 04 1, 063 , and 066 close FD Vessel fill stops Precoat Pump stans 064 and 070 open 063 opens Clean water from Precoat Tank is recircul ated through FD Vessel at low now rate.

Resi n Timer stans and is sealed-in 070 opens to high flo w setting Precoat recirculati on fl ow rate increases 053 open s 060 opens Slurry from Resin Tan k enters Precoat Pump suct ion th rough Resin Eductor Resi n Timer stan s and Res in Coating light comes on Resi n slurry pumped 10 FD Vessel where resin coats the FD sepia fo r 35 minutes 060 cl oses Resin slurry fl ow is shut ofTto Precoat Pump suction stream .

053 closes Resin Coating li ght goes out and Resin Timer resets 070 closes to low fl ow setti ng Precoa1 recircul ation fl ow rate decreases 062 opens and I-fold Pump stans Hold Pump supplies flow through FD Vessel 063 closes Precoat Pump supply to FD Vessel is shu1 ofT 064 & 070 close Backwash light comes on, Precoat light goes out, 058 FD inl et is lined up 10 FC or SF system opens, and Precoat Pump stops Backwash light goes out FD train is now in Hold mode and can be placed in service as needed . 36

TREQ 1648565-55 During shift in early September 2015 a leak was identified on the FC pool gate that separates the cask wash down pit from its adjacent pool. During initial investigation it was apparent that several operators were unaware of the capabilities or limitations of these pools and pits that are WEST of the 755' FB IFTS Fuel Transfer Pool. One knowledge deficiency in particular was that the fuel cask wash down area (pit) was not immediately recognized as NOT being a pool that would be capable of retaining fuel pool water if a seal failure were to occur. This information was either not covered or not retained by operators when the FC system review was performed. I do recall that there was some brief discussion about how the upcoming handling of casks may occur.

37

TREQ 1648565-55

/ GATE E STORAGE r GATE DSTORAGE GATE

+-D GATE GATE

-E C FUEt CA'S!<

S ORAGE POOL GATE C STORAGE SPENT FUEL STORAGE POOL GATE B STORAGE GATEA STORAGE L

RA: F POOL 38

CPS 3317.01 Task 331701.18 - Lower FC Surge Tank Leve*1 During System Operati_on Task 331701.30 - Pump Casing Vent After Maintenance for the Fuel Pool Cooling and Cleanup System CPS 3317.01 39

.OPEX Lesson Plan:

Attachment A- Fuel Pool Siphoning Events Attachment B - Reactor Cavity Overfilled during Floodup (Must-Know-OE) 40

Summary The purpose of the Fuel Pool Cooling and Cleanup (FC) System is to remove decay heat from the spent fuel assemblies, maintain pool water level, minimize fission product concentration in the water, and maintain pool clarity for fuel handling.

126 A HX FCPUMPA 004A FROM RHR RHR LC FCFILTER PUMP SUCTION 002 001 DEMINERALIZE B TO HX UPPER PCOLS 004 CASK P.:a SPENT TORAGE TRA.',;S."E."! FUEL POOL "°°'- POOL 41

.Diesel Genera tor/Diesel Fuel Oil -

Purpose

  • To provide an inde{Jendent, .Onsite source of Emergen cy Power during Loss of Off-site power and LOCA* to vital loads
  • Design Bases
  • Redundant - only need 2 of 3

~ Seismic

  • Enough fuel oil stored for 7 days at maximum DG load
  • Air starts- 5 consecutive starts without recharging air receivers
  • Start and load in 12 seconds .

Flow Paths

  • Fuel Oil Transfer and Storage

DAY TANK DIESEL GENERATOR STRAINER 55 PSIG FUEL OIL STORAGE TANK I_

Fig 17 FUEL OIL DRAIN TRANSFER PUMP n1cc,c1 l"'Ct..lCC, ft Tt'\C, C'I ICI t'\11 C>Tt'\C, ft t"'-C O TC, ft t..lC>C'CC, C>VC>TCIUI

INJECTOR INJECTOR FILTER FILTER INJECTOR ASSEMBLY 0--------

FUEL PRESSURE GAUGE FILTER ALARM (PANEL MOUNTED) SWITCH (50 PSI)

  • -----*-------- r i i i i' TO i DAY TANK i

i MANIFOLD i

'\I ASSEMBLY I FUEL PUMP i (ENGINE DRIV!=N) i FROM i DAY TANK i FUEL SUCTION i STRAINER i

i ii _ ........_ ........_______________________ _ FUEL PRIME PUMP Fig 18 DUPLEX FILTER

Fuel Oil Transfer Pumps

  • Located DG Bldg 712'
  • Takes suction on Fuel Oil Storage Tank
  • and discharges to Day Tank
  • Suction and Discharge pressure local indication
  • Auto start when DG starts and shuts down*

when DG does

Fuel Oil Day Tank

  • 737' DG Bldg
    • 1 hour1.157407e-5 days <br />2.777778e-4 hours <br />1.653439e-6 weeks <br />3.805e-7 months <br /> operation for max LOCA loads
  • Overflows back to storage tank
  • INOP DG for following levels
  • Div 1 & Div 2 <54%
  • Div 3 <35%
  • Low level alarm - local

Fuel Oil Storage Tanks

  • Stores and supplies of fuel oil to DG for 7 days during max LOCA conditions
  • Div 1 51,000 gallons (LCO limit is 43, 810)
  • Div 2 45,000 gallons (LCO limit is 38,572)
  • Div 3 29,500 gallons (LCO Limit is 25,286)
  • Level alarm local and indications in MCR

Fuel Oil Storage Tanks cont.

DC Priming Pump

  • Auto start on DG Start
  • Ensures sufficient fuel to injectors on DG Start
  • Auto stop when DG gets to 850 RPM (DIV 1 & 2)
  • DIV 3 runs continl.Jously
  • Local panel

Engine Driven Fuel on Pump

  • Driven by the engine accessory gear train
  • 4.5 gpm takes suction on day tank to injectors through filters
  • Supply and return header pressure near fuel oil duplex filter (local)

Fuel Oil Filters

  • Prevents clogging of injectors
  • One in service, other standby
  • Both can be in service with the selector lever in the mid-position

Starting Air

  • Starts and accelerat es the DG to achieve rated voltage, frequency and speed within 12 seconds of D_G start signal

275 PSIG 1DG16MC(G)

AIR COMP-RESSOR AIR MOTOR 1DG01CA (1DG02CA) AIR RECEIVER TANK s START SIGNAL 1DG640 CYL (1DG644) EN 1DG04TA 1DG16ML(N)

(1DG05TA) 1DG(

GOVERNOR BOOST AIR 1DG012D(H) MOTOR AIR MOTOR AIR DRYER 1DG21DA(B) 275 PSIG *I s START SIGNAL 1DG638 (1DG642) 1DG16MA(E) 1DG012C(G) 1DG16MB(F) 1DG012A{E)

GOVERNOR BOOST AIR MOTOR AIR AIR MOTOR RECEIVER 1DG008B(F) CYL TANK 1DG646B(F) OILER 1DG16MM(P) EN 1DG94TB s START SIGNAL 1DG639 AIR (1DG05TB) (1DG643) 1DG(

COMPRESSOR 1DG011A(C) 1DG01CB (1DG02CB) GOVERNOR BOOST 1DG16MD(H)

AIR.

Fig 18 1DG6.46D(H) .

1DG008D(H)

OILER MOTOR s START SIGNAL 1DG641 (1DG645)

GOVERNOR BOOST

250 PSIG 200 PSIG AIR COMPRESSOR AIR MOTOR 1DG03CA AIR RECEIVER TANK . s START SIGNAL AIR 1DG06TA MOTOR GOVERNOR BOOST 1DG012M 1DG012K CY E

1[

AIR DRYER 250 PSIG *I 1DG21DC 1DG012L AIR 200 PSIG MOTOR AIR MOTOR AIR 1DG008K OILER RECEIVER TANK s START SIGNAL-AIR 1DG06TB 1DG646K COMPRESSOR .

1DG011E GOVERNOR BOOST 1DG03CB Fig 19

DIV. I & II ENGINE AIR START MANIFOLD DIV. I & II ENGINE AIR START MOTOR Air Start Motors

  • Div 1 & 2 have three air start motors per engine
  • One of the motors on each engine is fed from the alternate air receiver
  • 6 motors engage and crank engine only three are required
  • Div 3 has 2 redundant pairs

Air Start Solenoids

  • Provide *the interface between the DG
  • starting control logic and the engine air starting system
  • Energized by 125 VDC
  • Manual override for a loss of DC
  • Air flow to air start motors through main air start valves from the receivers

In-Line Oilers

  • Installed in the air lines upstream of the air start motors
  • Release oil-air mist that lubricates the air start motors during engine cranking

Flow Path

  • Lube Oil

~ 1:::== - - - - ----;i,~

MAIN LUBE ~

I ===----======,

Fig 20

, PISTON -

COOLING-I I

TO TURBO FILTER BYPASS RELIEF VALVE MAIN LUBE AND 125psi 4 o psi SETPOINT PISTON COOLING PUMPS30-40ps id LUBE OIL FILTER 75 SCAVENGING PSI PUMP TURBO

[]FILTER LUBE OIL COOLER J CIRCULATING Cl;CULATING tIll OIL PUMP OIL PUMP 480 VAC 125 voe IMMERSION V TO HEATER MAIN BEARING HEADER TURBO TURBO SOAK BACK ENGINE OIL PUMP PUMP WATER _ __

480 VAC 125 voe OVERFLOW STRAINERO STRAINER ENGINE SUMP STRAINER SUMP

Vent To Engine

. --1 Cooling Wate

-===-===

~ections Fig 8 Lube Oil Cooler l

. ~

Lube Oil Circulating Pump Auxiliary Turbocharger 1 Lube Oil Filter Oit From Engine Sump Piston Cooling Oil Main Lube Oil And Oil To Bearings Piston Cooling Oil Pumps

Lube Oil Pumps

  • Main Lube Oil Pump: to engine moving parts 157gpm for 12 cylinder, 185 gpm for 16 cylinder
  • Piston-cooling Pump: to piston carrier to cool underside of piston crown and ring belt
  • 66 gpm for 12 Cylinder and 92 gpm for 16 Cylinder

Oil Pumps

  • Scavenging Oil Pump: provides suction pressure for main and piston cooling pumps
  • Goes through filters, cooler and strainer
  • Local discharge pressure

Circulating Oil Pump

  • AC driven keeps engine warm and ready to start
  • DC backup pump
  • On-Off Sw\tch at local engine panel

Turbo "Soakback Oil Pump"

  • 3 gpm
  • ON-OFF local controls

Lube Oil Strainers/Filters

  • 3 strainer: one is scavenging oil and 2 main lube oil
  • Lube Oil Filter: 7 element full flow type with sight glass on the side

Lube Oil Cooler

  • Cooled by jacket water and heated by jacket water
  • Inlet and outlet temperatures monitored locally

MCR CONTROL SW. LOCA RSP START TRANSFER SW. RSP EMERGENCY MCR START r - - -- TRANS FER SW. - ~

SELECT SW. NORMAL MCR CONTROL SW.

CONTROL MCR AUTO START SELECT SW. ROOM DIESEL ROOM LOOP LOCAL ENGINE START SW.

START AUTO START CIRCUIT 86 LOCKOUT RELAY LOCAL ENGINE MAINTENANCE SW.

START

MCR CONTROL SW. LOCA RSP S1ART TRANSFER SW. RSP EMERGENCY MCR START ,--- - TRANSFER SW. - -

SELECT SW. NORMAL MCR

  • CONTROL CONTROL SW.

AUTO

+-' MCR START SELECT SW. ROOM C DIESEL ROOM 0

u LOOP en

+-'

LOCAL ENGINE START SW.

START L.

co

+-'

en AUTO START CIRCUIT 0

+-'

s 86 LOCKOUT RELAY

<( LOCAL ENGINE MAINTENANCE SW.

START

DG Trips

  • Engine Over crank (failure to start but will cause a lock out relay trip) .
  • Low Lube Oil Pressure
  • High Water Jacket Temperature
  • Reverse Power
  • Loss of excitation
  • Overcurrent
  • Generator Ground Fault
  • Differential Overcurrent

DG Trips cont.

  • Engine Over crank (failure to start but will cause a lock out relay trip)
  • Low Lube Oil Pressure
  • High Water Jacket Temperature
  • Reverse Power
  • Loss of excitation
  • Overcurrent
  • Generator Ground Fault
  • Differential Overcurrent

Add/Remove Lube Oil Res ond to DG Auto Start Manual Override of Air Start Solenoids

Summary

  • Trips
  • Auto Starts

- Engine Overspeed - Division I & 11

- Engine Over crank (failure

  • High Drywell Pressure to start but will cause a lock (1.68 psig) and/or out relay trip)
  • Low RPV Water Level 1

- Low Lube Oil Pressure (-145.5")

- High Water Jacket

  • Bus Undervoltage Temperature

- b. Division 111

- Reverse Power

  • High Drywell Pressure

- Loss of excitation (1.68 psig) and/or

- Overcurrent

  • Low RPV Water Level 2

- Generator Ground Fault (-45.5")

(Div 1 & 2)

  • Bus Undervoltage 81

- Differential Overcurrent

Purpose

  • Ventilation for the three DG rooms, day tank rooms, and the FOST rooms (to prevent accumulation of diesel fumes).
  • Normal alignment for VD:

- Oil Room Exhaust Fans for all 3 DGs running (draw from the day tank and FOST rooms)

- Makeup Fans running

- Supply fans off

Design Bases

  • Operate under normal and abnormal plant operating conditions
  • Air intake and exhaust openings are located a sufficient distance apart to preclude reintroduction of exhaust air into the room
  • Seismic
  • Vital power
  • Divisional separation
  • Limit room to 130degF

Flow Paths CPS 3403 . 01 2.1 VD contro l s the temperature in the DG rooms due to equipment considerations . It also mainta i ns su f ficient air f l ow to the day tank and o i l storage rooms to keep the rooms purged of potentia l ly combust i ble fumes .

2.2 Normal system conf i gurat i on is wi th :

DG Rm lA(B) [C] Vent Fans , 1VD01CA(B) [CJ in STANDBY .

DG Vent Oi l Room lA(B) [C J Exh Fans , 1VD02CA(B) [C] running .

DG Make - Up Fans , 1VD03CA(B) runn i ng .

2.3 When any o f the DGs start , the associated vent f an a l so starts in antic i pation of the increased a i r flow and cooling requ i rements .

~ U PFAINA OD1ES8L ODIESE G EN E RA OR ROO?, GE ERATOR ROOM OD1ES 8L 1C 1B G BN E RATOR ROO' 1A DIESEL ,GE - RATOR R0 0 1 1 HVAC AK UP SYSTE .

1VD 01Y A

DlESELGIEINERATOIR IROO 1A ( 1B,1C )

1V010Y A(B,C)

IOAY TANK ROOMI 1A (1B,1C)

EXHAUST FA IETL 1VD08Y A (B ,C)

DIESEL G 1 RAT0 R 1

OL TANKROOIM V TSYS 1A ( 1B,1C)

Increasing Cooling

/Purge Mode 3403.01, Section 8.3 NOTE

  • DG Rm 1A(B)[CJ Vent Fan, 1VD01CA(B)[CJ will trip at -

70°F room temperature when the DG is not running.

  • Supply Air Damper 1VDO 1YA(B)(C) will not open on fan start if outside air temperature is < 70°F
  • When in PURGE mode, the supply air damper and recirc damper do not modulate to maintain > 70°F
  • The respective Diesel Generator Day Tank Room DP is impacted by running the VD Vent Fan for that division (especially Division 3). Alarms and auto start of the FO Transfer Pump have occurred upon VD Vent Fan start (IR 910035).

Increasing Cooling

/PURGE Mode 3403.01, Section 8.3 (Cont.)

WARNING

  • The starting of the DG Room Vent Fan can cause injury to any personnel located in the DG Vent Room.
  • Observe proper safety precautions for entering a CO2 filled atmosphere.
  • DG Rm lA (B ) [ C J Vent Fa ,. 1VD0 1CA(B,) [C J ..

Increasing Cooling/PURGE Mode 3403.01, Section 8.3 (Cont.)

( oca)

IF desired fo r te perat re/PURGE co t r o l ,

THEN pace Di v 1(2) [3] rge Switch to URGE.

v 1 3 ] at entrance to *v 1 3 ] DG Roo, v a CB, 755' HVAC Mezza 1 i ne , Y- 129 . )

3. i e l c r eased coo l i ng/P GE mode l S no o . ger des i red ,

- ) ( oca ) p ace l V ( 2) [ 3 J rge Swi tch to NORMA .

) (MCR) Stop DG A (B) [ C ] Ven t Fan, VDOlCA( B) [ C ]

  • CO2 Initiation 3403.01, Section 8.8 NOTE On a CO2 initiation signal, following divisional fans trip and dampers shut:
  • DG Rm 1A(B )[C] Room Vent Fan, 1VDO 1CA(B )[C]
  • DG Vent Oil Room 1A(B)[C] Exh Fan, 1VD02CA(B)[C]
  • DG Make-Up Fan A(B), 1VD03CA(B)
  • Makeup Fan Discharge Damper, 1VD25YA(B)
  • Filter Isolation Damper, 1VD18Y
  • Back Draft Damper, 1VD27YA(B)[C]
  • Fire Dampers 1VD08YA(B)[C] & 1VD1 OYA(B)[C]

CAUTION Observe proper safety precautions for entering a CO2 filled atmosphere.

CO2 Initiation 3403.01, Section 8.8 (Cont.)

r ._. :

I

1. .h en th ~02 I niti ti sig l .1.

1 ) Purg* A (B ) [ J p r s ti *3.

L.. ) a e Ma t e a ce e a e t. e f

  • e ,

f , - t J-_e f

. e -

l e a "'

1 1 0 . .A

') lV O ..:fB 3 1 _. Q Y

  • 1
  • J10 ..:fA 1 lOYB 1 _.10 .:fC

) ~t rt V per s tin * .1.

OPEX Beaver Valley Unit 1 2015-11-10 1:57 PM #320530 Failure of DG CO2 System to Actuate During Surveillance Testing Abstract:

On 11/10/15 during the 18 month surveillance test of the Unit 1 number 1 Diesel Generator CO2 system, the valves for the CO2 system did not actuate when tested from a Manual discharge pushbutton. In the event of a fire CO2 fire suppression would reduce the potential for damage to safety-related equipment important to safe shutdown. The cause was a pilot valve mechanical plunger became stuck.

Since a compensatory firewatch was established this event had minimal impact on station operations.

93

Summary

  • Rooms ventilated?

~ The three DG rooms, day tank rooms, and the FOST rooms

  • Normal alignment:

Doil Room Exhaust Fans for all 3 DGs running (draw from the day tank and FOST rooms)

D Makeup Fans running 0Supply fans off

  • Review flowpaths:

~ Normal Standby Mode

~ Diesel Generator Operating Mode

~ Purge Mode 94

BC081r4_Controllers 4. State the purpose of a controller.

A controller is device that compares input signal with setpoint and generates output based on difference (error signal)

Five types of controllers:

1. Two position controller
2. Proportional controller
3. Proportional plus derivative
4. Proportional-plus-reset controller
5. Proportional-plus-reset-plus-rate controller 96

BC081r4_Controllers 5. Describe the theory of operation of the following types of controllers:

Two position Two-Position Controllers The device has two positions: on or off The opening and closing of final control element results in cycling characteristic of measured variable ON WATER FLOW OFF -

TIME .

97

BC081r4_Controllers 5. Describe the theory of operation of the following types of controllers:

Proportional controller FULCRUM

---WATER IN 41N.-- /J\~ 41N.

//\\VALVE QIN.--

--WATER FLOAT OUT CHAMBER 98

BC081r4_Controllers 5. Describe the theory of operation of the following types of controllers:

Proportional plus derivative The proportional plus derivative (PD) controller or rate controller results in a more rapid response and less offset than the pure proportional controller.

99

BC081r4_Controllers 5. Describe the theory of operation of the following types of controllers:

Proportional-plus-reset controller Offset Error:

The difference between setpoint and measured variable is called "error" This error signal maintains control valve at specific position in response to change in demand of system Proportional-plus-reset controllers automatically reset measured variable to setpoint, thus, offset error is eliminated 100

BC081r4_Controllers 5. Describe the theory of operation of the following types of controllers:

Proportional-plus-reset-plus-rate controller To overcome disadvantages of Pl controller, "rate section" may be added 101

Valve Characteristics The flow characteristic of control valve is relationship between flow rate through valve and percentage of valve travel 3:

a. To compare and discuss flow 0

...J u.

characteristics of valve , it is helpful to ~

plot curve as percentage of travel versus percentage of flow

b. Th._e three most common flow characteristics are
  • Linear
  • Quick Opening 0 100
  • Equal Percentage  % SPAN OF POSITIONER OUTPUT PRESSURE 102

Valve Positioner The primary function of valve positioner is to maintain control valve disk at position that is directly proportional to its controller output pressure A valve positioner can be used to reverse signal to valve and to overcome frictional forces within valve on high-pressure drop applications.

Valve positioners are usually mounted on side of diaphragm actuators and on top of piston and rotary actuators HIGH PRESSURE PNEUMATIC SUPPLY Because of large volume of pneumatics required to operate valve, valve positioner has independent, regulated, pneumatic supply. FAIL CLOSED (normal seated valve)

Use of valve positioner should be considered for systems where it is necessary to provide control of process with minimum overshoot and fastest possible recovery following disturbance 103

Valve Positioner cont.

In many cases, valve positioner improves performance of process control loop Studies have shown that use of valve positioners is clearly beneficial in slow processes and clearly detrimental in fast processes use of valve positioner should be considered for systems where it is necessary to provide control of process with minimum overshoot and fastest possible recovery following disturbance HIGH PRESSURE PNEUMATIC SUPPLY FAIL CLOSED (normal seated valve) 104

1 PA05J controller operations (02422997-82)

MOVABLE SETPOINT / MEASURED Request: Training be VARIABLE INDICATOR SCALE performed for E0-1 and EO-C populations on 1PA05J MEASURED VARIABLE/

controller operations. ERROR POINTER

=60 SETPOINT THUMBWHEEL Newer equipment operators -=-so do not have full understanding -- FIXED SETPOINT of how to operate Bailey/NUS HAIRLINE controllers at the 1PA05J OUTPUT POINTER OUTPUT panel in a transient condition. SIGNAL METER MANUAL

~~PUSHBUTTON (Increase Output)

MANUAL e e AUTOMATIC INDICATING INDICATING LIGHT LIGHT MANUAL AUTOMATIC BUTTON BUTTON 105

Purpose of ES/HD To improve overall plant thermodynamic efficiency To route condensed Extraction Steam and non-condensable gases to the Main Condenser Primary method to drain moisture from the Main Turbine Design Bases To raise condensate/feedwater temperature from approximately 100°F leaving the Main Condenser to approximately 430°F prior to entering the reactor vessel, in order to improve overall plant efficiency.

107

Flowpaths Extraction Steam (fig. 1)

One class of Forty Six 7 th Graders ate ten dozen donuts 1 4 6 7 8 1Q 12 (TUREINE EXTRXTICN ST.llGES)

' \ ,'

,, /

HP LP TURBINE TUREINES GENERATOR SSE LP TURB) 12

( "A" ONLY CB PUMP S RE CO MB SJAE For the mathematically inclined:

SPE 1 +4 +6 = 11 10 + 2 = 12 6 + 5 = 11 12 + 1 = 13 CD PUMP S 7 + 4 = 11 8 + 3 = 11 CO NDENSER 108

Flowpaths cont.

Extraction Steam Normal Operation (One Heater String Shown) (fig. 2)

DCI'RACTION STEAM SOURCES FROM HPTURB 4111 STAGE (AND lSTSTAGEDR.AlNS) .AO lESOBA HPHEATER 6A TO

.__- - ~ - - -- ~ CONDENSER FROM HPTURB

.AO EXHAUST TOMSR lESOlcSA LP HEATER SA FROM LP TURB lB .AO AO MO 7TH STAGE lESOl6A 1ES033A 1ES009A LP HEATER 4A TO

'1:....---1_...___ _ _ _ _ _ _ _ _ _..,. CONDENSER 109

Flowpaths cont.

Extraction Steam Startup / Abnormal Operation (One Heater String Shown) (fig. 3)

EXTRACTION STEAM SOURCES FROM HPTURB 4THSTAGE (AND 1ST STAGE DRAINS) AO lESOBA HPHEATER 6A TO 1----C> CONDENSER FROM HP TURB EXHAUST AO TOMSR lES016A LPHEATER 5A TO CONDENSER FROM LP TURB lB AO AO MO 7TH STAGE 1ES026A 1ES033A 1ES009A LPHEATER 4A TO t----------------------c:=-- coNDENSER 110

Flowpaths cont.

Heater Drains Normal Operation (One Heater String Shown) (fig. 4)

Con de nse r Con de nse r Con de nse r Con de nse r Con de nser Con de nse r 111

Flowpaths cont.

Emergency Drains (fig. s)

REH EATER DRA IN TANK I A


**-*****-***-.. ------i P....------;-,.--; :::,,<: 1-- ~ TO CONDENS~R

,-**-**-***-***-***- -**-**- **-***-***-***-***-**-~

II  !* TO  :

I CONDENSER !

I L.._ +-l LP HEATER IA

............... : TO CONDENSE R TO CONDENSER TO CO DE SER TO CON DENSER 112

Components Feedwater Heaters MAIN CO NDENSER EATER OPERATIN G EATER DRAIN VENT OOOLER START-UP VE T HEATER

- - - - - - - - - . START-UP VENT CONDENSATE -- HOT DRAINS DIIVIDER OUT PLATE IN I BAFFLE SUB-COOLED DRAINS DRAIINS ATERS 2 6 CONDENSATE.

OUT IN 113

Components cont.

Flash Tanks 2A/B ES cs---~ ...-...........

LP Heat 1A/B 114

Components cont.

Drain Coolers DRAINS IN CONDENSATE _ __._

OUT CONDENSATE IN DRAINS DRAINS IN OUT CONDENSATE OUT DIVIDER PLATE CONDENSATE DRAINS IN OUT 115

Components cont.

Extraction Steam Isolation Valves FROM HPTURB 4TII 'STAGE

( AND lST 'SI'AGE DRAIN S) AO HPHEA'IER 6A 10 I - -...... CONDENSER 116

Components cont.

Extraction Steam Check Valves FROM LP TURB IB 101H STAGE FROM LP TURB IB 101HSTAGE TO CONDENSER SHAFT 0 CYLINDER PISTON ROD SPRING PULL DOWN BOLT 117

Components cont.

Heater and Drain Cooler Normal Drain Valves Normal Drain Valves Emergency Drain Valves Fail CLOSED on loss of air or power Fail OPEN on loss of air or power Auto CLOSE on high Auto OPEN on level in downstream high level in heater associated heater 118

Components cont.

Heater and Drain Cooler Emergency Drain Valves Normal Drain Valves Emergency Drain Valves Fail CLOSED on loss of air or power Fail OPEN on loss of air or power Auto CLOSE on high Auto OPEN on level in downstream high level in heater associated heater 119

Automatic Functio ns/ Interlocks

  • High Heater Level
  • High-High Heater Level

Evaluate Parameters'

1. Low heater level on system performance
2. Any heater reaching it's high level setpoint
3. High heater level on system performance
4. Any heater reaching it's high-high level setpoint 121

Evaluate Parameters cont.

5. Heater string isolation valve closure
6. Loss of control power
7. Effect on other heaters when heaters are removed from service/ returned to service 122

8.3.1 Feedwater Heater Abnormal Level CAUTION <<CM-7>>

A Low level in the heater may cause level to be too near the bottom of the "snorkel" which will 310201.16 introduce a possible steam path into the drain cooler which would cause increased vibration and would lead to tube damage. See Appendix F: Feedwater Heater Distance To Snorkel.

Time spent with a low heater level must be minimized to reduce the potential for heater tube damage.

Respond to. Highfeedwater heater levels cause extraction steam valves to the respective heater to close. If this occurs, refer to CPS 4005. 01, Loss ofFeedwater Heating while continuing in this procedure.

Feedwater NOTE Heater See Appendix B, HEATER VALVE LISTfor valve numbers associated with each heater vessel.

Emergency drain valve controller output is" 100%for valve fully closed.

Abnormal Level Normal drain valve controller output [s 0%for valve fully closed.

1. IF Feedwater Heater Abnormal Level is result of a system malfunction or FW heaters are not operating properly, THEN
1) Refer to CPS 4005.01, Loss Of Feedwater Heating for possible entry*conditions.
2) As necessary to help determine heater level high or low, use Appendix G, Feedwater Heater Level Diagnostics.
3) Determine which drain control is malfunctioning, and if necessary, take manual control of the valve.
4) If normal drain valve control is malfunctioning, it will be necessary to reduce the emergency drain setpoint in order to maintain relatively normal heater level.

In this case, normal drains should be positioned in manual to maintain as little flow as practical through the emergency drains.

5) If any heater controls are left in manual, the controls should be checked frequently due to the possibilities of controllers drifting in manual and due to changing demands that occur with123 small load changes.

310201.16 8.3.1 Feedwater Heater Abnormal Level (cont'd)

Respond to 2. IF Feedwater Heater Abnormal Level is result of a plant manipulation 9r transient Feedwater THEN (i.e., bypass valve operation, removal/

restoration of FW Htrs, etc.) , <<CM-6>>

Heater After stabilization of the feedwater heaters, verify proper operation of the feedwater heaters:

1) Normal level being maintained. (P680/1PA05J).

Abnormal Level 2) Normal and Emergency Drain Controllers operating properly.

cont. 3) 4)

ES isolation valves positioned correctly.

FW heater bypass valves positioned correctly.

5) BOP-5 video services parameters indicate normal values.
6) Feedwater temperatures are normal.

NOTE JCB003A(B) and JCB005A(B) isolate (close) on Flashtank high level.

If condensate flow is attempted to be restored with Flash tank high level sensed, the heater isolation valves (JCB003A(B) & 5A(B)) will stroke open then immediately closed.

124

CAUTION Section 8.2.3.1 shall be reviewed prior to proceeding due to changes infeedwater heating.

310201.19 8. 3. 4 Preparing Feedwater Heater Level Control For Maintenance Or Trouble-Shooting Of A Normal Drain Valve Malfunction Preparing 1. At panel 1PA05J, verify level indicating cont.roller for the emergency level control valve is in AUTO, and Feedwater Heater controlling at a reduced setpoint as described in 8.3.1.1.3.*

Level Control For 2.

3.

Verify/place the normal drain*controller in MANUAL.

Slowly close the normal drain valve using the closed Maintenance Or push button on the level indicating controller while observing that the emergency level controller responds to maintain heater level.

Trouble-Shooting 4. IF THEN Necessary due to the malfunction, Of A Normal Drain 1) Isolate the malfunctioning drain valve.

(refer to Appendix B Table 1 for list of normal drain isolation valves)

Valve Malfunction 2) Ensure the emergency level controller is maintaining heater level as desired on emergency level indicating controller.

5.* WHEN Trouble-shooting/maintenance is complete, THEN Ret1.hn normal drain regulator to service by performing the following as appropriate:

1) Appropriate portion of CPS 3102.01V002, Heater Drains Valve Lineup completed (if needed).
2) Appropriate portion of CPS 3102.01V004, Heater Drain Instrument Valve Lineup completed (if needed).
3) Open the heater normal drain valve until the emergency drain automatically closes, and place the normal drain valve in automatic.
4) Restore the heater emergency drain controller setpoint to its nominal value.

125

Radwaste l

  • All solid RW processing tanks contain a "plumb-bob" type level measuring.
  • Operated from the Quantum Master Control cabinet
  • One type of plumb-bob is used for decant water level and another type for sludge level.
  • Each plumb-bob has a separate operating mechanism; therefore there are two separate mechanisms o,n top of each sludge tank.
  • Concentrate Waste Tanks are the e;xcepfion; there is only one mechanism to measure total level in these tanks.

(Concentrated Waste Lesson Plan, LP85492) "\

127

e.

. ~

~ ,. t' l:i:I

  • All solid RW processing tanks contain a "plumb-bob" type level measuring.
  • Operated from the Quantum Master Control cabinet
  • One type of plumb-bob is used for decant water level and -

another type for sludge level.

  • Each plumb-bob has a separate operating mechanism; therefore there are two separate mechanisms on top of .

each sludge tank.

  • Concentrate Waste Tanks are the exception; there is only one mechanism to measure total level in these tanks.

(Concentrated Waste Le~son Plan, LP85492) 128

Open LP and review Figures 11~11 Course/Program: ' ILT/NLO/LORT Module/LP ID: N-CL-OPS-268016

Title:

" SOLID RADWASTE SLUDGE Course Code: N-CL-OPS-268016 COLLECTION/DISPOSAL SYSTEMS Author; Russ Werman Revision/Date: 01 I 08102112 Prerequisites: Revision By: M. Rodin Est. 'Teach Time: 3.0 hours0 days <br />0 hours <br />0 weeks <br />0 months <br /> Qualified Nuclear Eniineer NIA NIA Review (If applicable): - Date:

Trainimz Suoervisiori Review: W. D. Kiser ISi . Date: 08109/12 ProJ!.ram Owner Aooroval: Rick Bair ISi Date: 08/15112 r**--------- --**r*-*--*-**---. --- TABLEOF*CONTENTS _____ ------*T Pg.#--:

I. INTRODUCTION ............................................. , .................................................................................................................. 1 A TOPIC lmRODUCTION .. ..................................... . . ............. 1 B. OVERVIEW OF TRAINING SESSION ............. . .. ..................... 2 C. EVALUATION *..*.*....*..*..*..*.............*..*.............*... ...2 D. MANAGEMENT E.XPECTATIONS ......*.....*............. .......... 3 II. SYSTEM PURPOSE/DESIGN BASIS ............................................................................- .................................................. 4 A

B.

SY~i'!Thl PURPOSE .......................................... .

DESIGN BASIS ................................................... .

................................................. 4 Ill. SYSTEM FLOWPATH(S) .............................................................................................................................................. 5 A. SYSTEM OVERVIEW ....................................................................................................................................................... 5 B. WASTE SLUOOE TANK INPUTS................... ............................................................. ........ 5 C. REt\CTOR WATER CLEANUP (RT) SYSTEM BACKWASH RECEIVING TANK............. ............................ ............. 6 D. DECANT................................................................... .......................................................... .. ........ 6 E. BOTIO~I STIR. ................................................... . ......................................................................................... . .... 7 F. MOBILE SOLIDIFICATION ..................................................................................................................................................... 7 IV. COMPONENTS_ ............................................................................................................................................................. 8 A. PIIASE SEPARATOR SLUDGE TANKS. .. ................................................................................................... 8

8. FUEL POOL FILTERIDEMINERALIZER SLUDGE TANKS .. .................................... ...................................................... 8 C. WASTE SLUDGE TANKS....................................................................................... ..... 9 D. BACKWASIIRECEIVINGTANK.................................. .................................... .................................................... .. ....... 9 E. SY~'Tf~I PUMPS ................................................................................................................................................................... 10 F. POWER SUPPLIES............................................... ............................................ .. ..................................... 11 V. INTERLOCKS ..- ........................................................................................................... _.................................................... 12

© Copyright 2007 by fa:clon Nuclear, AH Ri(!hts Reserved. Pennission for reproduction and use is rcscn*cd for Exelon Nuclear.

(Any other use or reproduction is c:,;prcssly prohibited without the express permission of Exelon Nuclear.)

129

Attach ment A RW Basement Flooding From Stuck Open Condensate Filter Demin Vent Valve Cmirse/l'rogrnm: ILT/NLO/LORT *Module/LP JD:* N-CL-OPS-268016

Title:

c,SOUDRADWASTESLUDGE CourseCudc: . N-CL-OPS-268016 COLLECTION/DISPOSAL SYSTEMS Author: Russ Wcm1un Revision/Date: 01 / OR/02/12

  • Pri.'11:quisitcs: Rtwision B)~ M. Rodin
  • Est. Tcach Time: 3.0 hours0 days <br />0 hours <br />0 weeks <br />0 months <br /> QUulified Nucle:irEnginccr IN/A ,\NIA Review(Irannlico.ble): Date:I Trdinin 'Su ervision Review:* 'I W. D. Kiser /S/ Date: I OR/09/12 l;ro ram Owner Arinmval: I Rick Bair /S/ Date: I OR/15/12 r . . . .-------**1 **----*-** TABLEOFCONTEl\'TS ---------*11*g.#*-1 I. LYTRODUCTIOX.---**-----*-------------*-*----*-*-- -*-**--***-***********-* 1

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V. INTERLOCKS Cl Copyright 2007 by Exi:lon Nu,;kar, ,\1111.ight* Reserved. Fmnission for rq,mduction and use i* reserved for Exelon Nuckar,

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Phase Separators - 3909.02 D iscussion 1

The Phase S~parators collect waste sludge from the Reactor

. ~'Jater Clean Up Fi 1 ter Demineraliz er Backwash Receiving Tank.. After a sufficient volume of slu,dge has- been accumulated , tank contents are decanted, recirculated and transferred to a Vendor for processing. Once tank contents have b*een transferred , the tank an*d associated components are flushed to remove sludge residue. Tank recirculatio n is normally performed manually. Flushing 0£ the tank ~nd associated components is also performed manually ..

Operation of the Phase Separator Sludge System to transfer sludge for processing will be a coordinated evolution bet,ueen Operations and Vendor.

131

Phase Separator Lvl Reading I BlflBENCE BBi I CPS 3909.02 8.6 Level Readings using the Console Quantum Master Control CAUTION If OLIX-fiVX511~ Console Quantun11vfaster Control, is activated 11.,hile the tank is in the recirculation n1ode or receiving 1vaste, the plu,nb-bob level sensor unit could be daniaged 8.6.1 Verify no anticipated waste inputs for the duration of the level r~ading e~olution.

8.6.2 Ensure tank is not in the Recirculation mode.

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132

Phase Separator Lvl Reading (Cont.)

8.6.3 Perform the following at OLIX-WX511, .console Quantum Master Control.

1. Depress.the F button until -display reads READ CHANNEL.

NOTE It ,nay take up to eight hours ofsettle tbne for the 1nost accurate sludge level readings.

2. *select applicable channel number from Table 1.

Table 1 Channel.No . Description 13 1WX03T Liquid Level 14 1WX03T Sludge Level 8 2WX03T Liquid Level 9 2WX03T Sludge Level J

Phase Separator Lvl Readingl  !

(Cont.)

NOTE Level reading is a one-tin1e reading, not a continuous input t;pe. Plunib Bob is still retracting vv*hen a reading appears on the display,* therefore, 40 not atte1npt to read any other channels

  • until the display sho1-vs "Ready and Tinie n. The conversion of level readings to indicate other than in feet can be perfonned.
3. Depress the E button.
4. To get the Console Quantum Master Control level readout to indicate other.than in feet, perform the following:
1. After performing a normal input sequence and while the readout is still indicating a level in feet, repeat.the_ F/_CHANNEL No./ E sequence two to four more times as desired.
2. A second sequence gives ALARM OF CHANNEL# (alarms are not actually hooked up so whether the readout says yes or no the answer is no)*.
3. A third sequence gives MATERIAL% OF CHANNEL#.

Lvl Reading (Cont.)

NOTE If the tank had been in recirculation and it is desired to take a sludge reading, it nuiy take up to eight hours for the sludge to settle. Th.erefore any readings before eight hours could be inaccurate.

4. A fourth sequence gives MATERIAL HEIGHT OF CHANNEL

=ff= (feet-again) . ,

5. A fifth sequence gives QUANTITY OF CHANNEL#

(gallons/cu. ft.).

No. OF SEQUENCE READOUT 1 Feet 2 Alarm I

3 Material 96 I

I J

4 Feet L 5 Gallons/ Cu. Ft.

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,I I! 8. 21 Resetting a Locked Up Quantum Master Controller CPS 3909.02 NOTE A sche1naticfor the Quantuni .11daster Controller is located in K-WX-FOJ0-001 Bulletin 503.

There is only one fi1se inside the Quantun1 Master Controller cabinet.

8.21.1 Obtain SMngt authorization to reset the locked up Quantum.

Master Controller.

8.21.2 *open the Quantum Master Controller cabinet on OPL08J.

8.21.3 Using the proper electrical safety precautions per SA-AA-1?9, remove the unlabeled 5 amp fuse located inside the top center of the Quantum Master Controller cabinet.

8.21.4 Re-install the 5 amp fuse removed in the previous step, 8.21.3.

':8.21.5 L_

Close the door to the Quantum Master Controller.

136

Actions for quantum master controllers are the same for.:

Task 390903.02 - Waste Sludge Tanks level readings Task 390904.03 - Concentrated Waste Tanks l~vel readings

  • Also secure the applicable tank agitator
  • Task 390905.02 - FP/FD Sludge Tanks level readings 137

Purpose of Spent Resin Sys

  • To receive expended resi,n -slurry from the Condensate Polishers, the Radwaste Demineralizers, and charcoal from the Radwaste Demineralizers.

138

OWX04T Ill Get Liquid Depth Decant Line Last Sludge MeasureMent

Get Sludge Depth 1r<<-1~11a~=1*1 I

l! D-5 .38 Feet I!

LIQUID & SLUDGE MEASUREMENTS CANNOT 139 Home BE TAKEN SIMULTANEUOSLY

140 Spent Resin Tank-level readings Task 390901.02 - Resetting a Locked Up Quantum Master Controller WX Level Control PLC Section 8.18 CAUTION To prevent possible darnage to OLIX-FVX513, PVX Level Control PLC, 1.vait 10 seconds after renloving po1ver before applying po1ver again.

8.18.1 Obtain Shift Management authorization to reset *1ocked up 0LIX-WX513, WX Level Control PLC.

8.18.2 Open the back panel door on OPLOBJ to obtain access to the back side of OLIX-WX513, WX Level c*ontrol PLC.

8.18.3 Use the proper electrical safety precautions per SA-AA-12 9, Electrical Safety, for the folln-;;11,ring steps.

8.18.4 Locate the green 3-position power terminal block connector located o~ the back side of OLIX-WX513, WX Level Control PLC, in ttie lower left hand corner on the controller.

141

Spent Resin Tank-level readings Continued ...

8.18.5 Remove the green 3-position power terminal block connector by pulling down on the connector until it is removed from the controller.

8.18.6 Wait a minimum of 10 seconds before proceeding.

8.18.7 Install.the green 3-position power terminal block connector by pushing up on the connector until it is seated in the controller.

8.18.8 OLIX-WX513, WX Level Control PLC, will now go through a power on initialization sequence and then display the Home Screen.

142

Improper Loading of Resin IR 02666117

  • On 5/6/16 as identified in IR 2666117, resin was,improperly loaded ilito WE demin "C" per 3906.01. 1*5 barrels of anion and 5 barrels of cation were loaded. The .

proper amount of resin is 13 barrels of anion and 5 barrels of cation (per section 7.1) 143

  • Improper Anion Underlay Resin Load (CP 'E')

IR 02673997 on 5/18/16 Required Load Loaded

  • Anion underlay -
  • Anion underlay loa*ded

- 20 barrels A-284-LS - 4 barrels A-284C (20cf)

(1 OOcf). and 16 barrels A-284-LS

  • Mixed bed portion * (80cf)

- 11 barrels cation C-471

  • Mixed bed portion loaded.

(55cf) and 8 barrels anion - 11 barrels cation C-471 A-284C (55cf)

- 4 barrels anion A-284C

- 4 barrels A-284-LS 144

WASTE DEMINERALIZER Figure 2 WATER INLET UPPER

/ DISTRIBUTOR REGENERANT DISTRIBUTOR INTERFACE COLLECTOR V!lffllll!ll#llll!l#/1&$ff/,l@#I/Effl1 INTERMIXED CATION W!lll!lllliWll!#f§l$t1f'm11!11,f/JJ1 UNDERDRAIN AND ANION RESIN ASSEMBLY FALSE BOTTOM 145 WATER OUTLET

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ischarge I I

  • Large volumes of water will require* processing and dispositioning to support station shutdown and decommissioning of statipn systems.
  • During review of decommissioning activities for Clinton Power Station, it has been identified that returning ORIXPR040, Liquid Radwaste Discharge monitor to, service to support potential liquid discharges from the station may be warranted.
  • 9911.50 - Liquid Radioactive Discharge Surveillance

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Summary

  • Tank Level Readings
  • Importance of proper resin loads
  • Liquid RW discharge 147

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL} Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Using normally available references, unless otherwise stated, and with 100°/o accuracy, in accordance with course reference materials and procedures, the trainee shall:

Objective Description ~ Slide(s) 233000.1.1 - STATE the purposes of the Fuel Pool Cooling & Cleanup System 20-22 including applicable design bases.

233000.1.2 - Describe the major flow paths for the following modes of the FC 23-29 system

.1 Normal _Flow path

.2 RX vessel pool draindown

.3 RX vessel pool fill

.4 FC assist

.5 Alt Suppression pool cooling 31 233000.1.6 - Given a Fuel Pool Cooling& Cleanup System Annunciator, DESCRIBE: 32

b. Any automatic actions 233000.1.7 - Given the Fuel Pool Cooling & Cleanup system, DESCRIBE the 33-36 systems supporting and the nature of the support.

233000.1.15 - Given Fuel Pool Cooling & Cleanup System initial conditions, PREDICT how the system and/or piant parameters will respond to the manipulation of the following controls_.

.2 Fuel Pool Cooling & Cleanup system Filter/Demin controls for Hold, Filter, Backwash and Precoat

Lesson

Title:

2017 Cycle 1 Training {DG-DO, ES~HD, FC, RW, VD, TREQs, Mods & LL} Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Using the approved procedure, DISCUSS:

~ Slide(s)

Task 331701.18 - Lower FC Surge Tank Level During System Operation 39 Task 331701.30 - Pump Casing Vent After Maintenance for the Fuel Pool Cooling 39 and Cleanup System

(

Lesson

Title:

201TCycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Using normally available references, unless otherwise stated, and with 100% accuracy, in accordance with course reference materials and procedures, the trainee shall:

Objective Description ~ Slide(s) 264000.1.1 - STATE the purpose(s) of the DG/DO System including applicable 43-44 design bases.

264000.1.2 - Describe the major flow paths for the following modes of the DG/DO 45-4 7, 52-66 system

.1 Lube Oil Sys

.2 Fuel Oil Sys

.3 Air Start Sys 264000.1.5 - Discuss the DG/DO system automatic functions/interlocks including 48-51 purpose, signals, set points, sensing points, when*bypassed, how/when they are .

.6 Fuel Oil Storage Tank

.7 Fuel Oil Day Tank

.8 Fuel-Oil Transfer Pump 264000.1.7 - Given the DG/DO system, DESCRIBE the systems supporting and 74-75 the nature of the support .

.1 DG Auto Starts

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Using normally available references, unless otherwise stated, and with 100% accuracy, in accordance with course reference materials and procedures, the trainee shall:

Objective Description ~ Slide(s) 264000.1.11 - EVALUATE given key DG/DO System parameters, if needed 76-77 DETERMINE a course of action to correct or mitigate the following

_abnormal condition(s): .

. 1 High Crankcase Pressure

.2 Overspeed

.3 Overcrank

.4 Low Oil Pressure

.5 High Water Temperature

.6 Reverse Power

.7 Loss of Excitation

.s* Overcurrent

.9 Generator Ground Fault

.10 Differential Current

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Using the approved procedure, DISCUSS:

Task Description ~ Slide(s)

Task 350601.17 - Diesel Engine Lube Oil Addition or Removal 78 Task 350601.27 - Respond to DG 1A(18)[1 CJ Auto Start 79 Task 350601.34D - Alternate Diesel Generator Start - Manual Override of Air 80 Start Solenoids

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Using normally available references, unless otherwise stated, and with 100% accuracy, in accordance with course reference materials and procedures, (he trainee shall:

Objective Description ~ Slide(s) 233000.1.1 - STATE the purpose(s) of the DG ROOMS .HVAC System including 83-84 applicable design bases.

233000.1.2 - Describe the major flow paths for the following modes of the DG 85-87 ROOMS HVAC system operation .

. 1_ Normal Standby Mode

.2 Diesel Generator Operating Mode

.3 Purge Mode

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Using the approved procedure, DISCUSS:

Task Description ~ Slide(s)

Task 340301.03 - Increased Cooling/PURGE Mode of the VD System 88-90 Task 340301.08 - Respond to a CO2 Initiation with respect to the VD System 91-92

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lessor:, ID: N-CL-EOC-1701 Objectives Upon completion of this chapter, the student will be able to perform the following objectives at a minimum proficiency level of 80%, unless otherwise stated, on an oral or written exam:

Objective Description ~ Slide(s)

BC081r4_Controllers 4. State the purpose of a controller. 96 BC081r4_Controllers 5. Describe the theory of operation of the following types of controllers:-

97-101 *

a. Two position *-
b. Proportional
c. Proportional-plus-reset (Pl)
d. Proportional-plus-reset-plus-rate BC081r4_Controllers 7. Describe the following characteristics of a flow control valve: 102
a. Linear
b. Quick opening
c. Equal percentage BC081r4_Controllers 9. State the function and describe the characteristics of valve *positioners. 103-104 Treq 02422997-82 Discuss the operation of Bailey/NUS controllers at 1PAOSJ. 105

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, M0ds & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Upon completion of this chapter, the student will be able to perform the following objectives at a minimum proficiency level of 80%, unless otherwise stated, on an oral or written exam:

Objective Description ~ Slide(s) 239003.1.1 STATE the purpose(s) of the EXTRACTION STEAM, HEATER VENTS & DRAINS System including 107 applicable design bases.

239003.1.2 DESCRIBE the major flowpaths for the following modes of the EXTRACTION STEAM, HEATER VENTS & DRAINS System operation .

108-113

.1 Extraction Steam System while operating in the normal mode

.2 Extraction Steam System while operating in a specified abnormal mode

.3 Feedwater Heating Drain System while operating in the normal mode

.4 Feedwater Heating Drain System while op~rating in a specified abnormal mode 239003.1.3 DESCRIBE the function, operation, interlocks, trips, physical location, and power supplies of the following EXTRACTION STEAM, HEATER VENTS & DRAINS System components . 114-119

.1 Feedwater Heaters

.2 Flash Tanks

.3 Drain Coolers

.4 Extraction Steam Isolation Valves

.5 Extraction Steam Check Valves

.6 Heater and Drain Cooler Normal Drain Valves

.7 Heater and Drain Cooler Emergency Drain Valves

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Upon completion of this chapter, the student will be able to perform the following objectives at a minimum proficiency level of 80%, unless otherwise stated, on an oral or written exam:

Objective Description ~ Slide(s}

239003.1.5 Discuss the EXTRACTION STEAM, HEATER VENTS & DRAINS system automatic functions/interlocks including purpose, signals, set points, sensing points, when bypassed, how/when 120 they are.

239003.1.11 EVALUATE given key EXTRACTION STEAM, HEATER VENTS & DRAINS System parameters, if needed DETERMINE a course of action to correct or mitigate the following abnormal condition(s): 121-122

.1 Low heater level on system performance

.2 Any heater reaching it's high level setpoint

.3 Hig.h heater level on system performance

.4 Any heater reaching it's high-high level setpoint

.5 Heater string isolation valve closure

.6 Loss of control power

.7 Effect on other heaters when heaters are removed from service/ returned to service Task 310201.16 Respond to Feedwater Heater Abnormal Level 123-124 Task 310201.19 Preparing Feedwater Heater Level Control For Maintenance Or Trouble-Shooting Of A Normal Drain Valve Malfunction 125

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Using normally available re_ferences, unless otherwise stated, and with 100% accuracy, in accordance with course reference materials and pro~edures, the trainee shall:

Objective Description [ Slide(s) 268013.1.1- STA TE the purposes of Spent Resin System 138 268016.1.4- STATE the physical location and function of the following SOLID 127-130 RADWASTE SLUDGE COLLECTION/DISPOSAL system controls, indicators, and/or sensors .

.9 Quantum Master Control Console

.10 Tank Level Instrumentation 145 268009.1.10- EXPLAIN the reasons for given RADWASATE DEMINERALIZERS System operating limits and precautions

.1 Reason for maintaining Resin Outlet Valve gagged shut during normal operations:

  • .2 Method of performing a Resin/Charcoal load .

. .3 Method of performing a Resin unload .

.5 Loading charcoal prior to loading resin.

/

Lesson

Title:

2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Exelon Generation Lesson ID: N-CL-EOC-1701 Objectives Using the approved procedure, DISCUSS:

~ Slide(s]

Task 390901.02 - Spent Resin Tank-level readings, 17 Resetting a Locked Up 141-142 Quantum Master Controller Task 390902.06 - Phase Separators Level Readings 131-137 Task 390903.02 - Waste Sludge Tanks level readings 137 Task 390904.03 - Concentrated Waste Tanks level readings 137 Task 390905.02 - FP/FD Sludge Tanks level readings 137 TREQ 02623308 Liquid RW Discharge Surveillance 146 TREQ 02623308 Resin Loading activities 143-144 TREQ 02623308 WX Tank Level Mod 139-141

Questions 160

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