ML18360A476

Attachment 8: 2017 Training Material on Diesel Generator Air Start Flow Plow

ML18360A476
Person / Time
Site:	Clinton
Issue date:	12/14/2018
From:	Exelon Generation Co
To:	NRC/RGN-III, Office of Nuclear Reactor Regulation
Shared Package
ML18360A500	List: ML18360A469 ML18360A470 ML18360A471 ML18360A472 ML18360A473 ML18360A474 ML18360A475 ML18360A476 ML18360A477 ML18360A478 ML18360A479 ML18360A480 ML18360A481 ML18360A482 ML18360A483 ML18360A484 ML18360A485 RS-18-146, Evaluation of Preliminary White Finding
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) . 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 233000.1.1

-STATE the purposes of the Fuel Pool Cooling & Cleanup System including applicable design bases. 233000.1.2

-Describe the major flow paths for the following modes of the FC system .1 Normal Flow path .2 RX vessel pool draindown

.3 RX vessel pool fill .4 FC assist .5 Alt Suppres~ion pool cooling 233000.1.6

-Given a Fuel Pool Cooling& Cleanup System Annunciator, DESCRIBE:

b. Any automatic actions 233000.1.7

-Given the Fuel Pool Cooling & Cleanup system, DESCRIBE the 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

• Slide(s} 20-22 23-29 31 32 33-36.

Lesson Title_: 2017 Cycle 1 Trainin*g (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Lesson ID: N-CL-EOC-1701 Objectives Using the approved pro'cedure, DISCUSS: 1 Task 331701.18

-Lower FC Surge Tank Level During System Operation Exelon Generation Slide(s) 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) 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 264000.1.1

-STATE the purpose(s) of the DG/DO System including applicable design bases. 264000.1.2

-Describe the major flow paths for the following modes of the DG/DO 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 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 the nature of the support . . 1 DG Auto Starts Slide(s) 43-44 45-47, 52-66 48-51 74-75 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 264000.1.11

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

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 the approved procedure, DISCUSS: Task Description Task 350601.17

-Diesel Engine Lube Oil Addition or Removal Task 350601.27

-Respond to DG 1A(18)[1 C] Auto Start Task 350601.34D

-Alternate Diesel Generator Start -Manual Override of Air Start Solenoids Slide(s) 78 79 80 .,

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 233000.1.1

-STATE the purpose(s) of the DG ROOMS HVAC System including applicable design bases. 233000.1.2

-Describe the major flow paths for the following modes of the DG ROOMS HVAC system operation . . 1 Normal Standby Mode .2 Diesel Generator Operating Mode .3 Purge Mode J Slide(sj 83-84 85-87 Lesson Title: 2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & Lt) Lesson ID: N-CL-EOC-1701 Objectives Using the approved procedure, DISCUSS: Task Description Task 340301.03

-Increased Cooling/PURGE Mode of the VD System Exelon Generation Task 340301.08

-Respond to a CO2 Initiation with respect to the VD System Slide(s) 88-90 91-92 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 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 BC081r4_Controllers

4. State the purpose of a controller.

BC081r4_Controllers

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

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: a. Linear b. Quick opening c. Equal percentage BC081r4_Contrqllers

9. State the function and describe the characteristics of valve positioners.

Treq 02422997-82 Discuss the operation of Bailey/NUS controllers at 1 PA05J. Slide(s} 96 97-101 102 103-104 105 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) Lesson ID: N-CL-EOC-1701 Exelon Generation 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 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 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):

.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 Task 310201.19 Preparing Feedwater Heater Level Control For Maintenance Or Trouble-Shooting Of A Normal Drain Valve Malfunction Slide(s) 120 121-122 123-124 125 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 268013.1.1-ST A TE the purposes of Spent Resin System 268016.1.4-STATE the physical location and function of the following SOLID RADWASTE .SLUDGE COLLECTION/DISPOSAL system controls, indicators, and/or sensors . . 9 Quantum Master Control Console .10 Tank Level Instrumentation . 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. Slide(s) 138. 127-130 145 Lesson Title: 2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Lesson ID: N-CL-EOC-1701 Objectives Using the approved procedure, DISCUSS: Exelon Generation Task 390901 ~02 -Spent Resin Tank-level readings, 17 Rese_tting a Locked Up Slide(s) 141-142 Quantum Master Controller , Task 390902.06

-Phase Separators Level Readings Task 390903.02

-Waste Sludge Tanks level readings Task 390904.03

-Concentrated Waste Tanks level readings Task 390905.02

-FP/FD Sludge Tanks level readings TREQ 02623308-33

-Liquid RW Discharge Surveillance TREQ 02623308-21

-Resin Loading activities TREQ 02623308-01

-WX Tank Level Mod 131-137 137 137 137 146 143-144 139-141 Lesson Title: 20i7 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL} Lesson ID: N-CL-EOC-1701 Exelon Generation 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) 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 Exelon Generation

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) 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 Exelon Generation 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 E@ Pagers and phones on silent mode Practice good housekeeping 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 RHR P UMP SUCTION Flow Paths FROM U PPER POOLS FC FILTER 023 CAS K 10RAGE POOL A HX B HX SPE T F U B.. POOL FRO M RHR TO UPPER POO LS 23 CY~ Makeup GJB RHR -Pump LC Suction 002 001 A Surge Tank From CNMT Upper Pools 035 014A FCPump~-0 FC Pump 8 0148 1FC133 ______ _, i---t .... t--1 Cask 5 orage 1FC127B P oo l To Fuel Building Equipment Dra i n Tank 1R E 01T < Normal FC A Hter Dem i neralizer Fue l T r an sf e r Po o l 023 1FC127D 024A 1 A HX l FC OlAA B HX l FCO lA B l l 026A From RHR 0268 FUEL POOL COOLING AND CLEANUP SYSTEM FLOW DIAGRAM To CNMT Upper Pools To Equipment Drains RX vessel Pool Draindown FRO M FC S U PP LY 1 57 CNMT BOUNDARY f t t t t .--------~ -* -----, 3 1 11 FROM 3A RHR ___ , 1 56 FROM I 3 f B RHR 38; I I 86B t I I I I I ' ! :r r FC SYSTE M FLO W D I AGRAM CON T A IN ME NT POOLS T O C OND E N SE R I CNMT BOUNDARY 1 36 FILL LJNE FR O M C Y :~0-1 CY0 1 0 T O FC S U RGE T A NK S 25 RX vessel Pool Draindown CY~ Makeup G.38 RHR -Pump Suct i on 002 00 1 T o Fue l Bu il d i ng Equ i pment Dra in T ank 1RE01 T A B Surge Tank F rom CNMT U pper P , oo l s 0 1 4A F CPum p~-0~ 1 FC004A 0 1 6A FC Pump B C a sk s or age 1 FC127B Pool .--------, FC R.il ter Fu e l T ransf e r Pool 023 1 FC 127D 0 24A 1 A HX l.FC OlAA B H X l F COlAB Sp e n Fu e l stor age Pool l l 026A 026B FUEL POOL COOLING .AND CLEANUP SYSTEM FLO\N DIAGRAM From RHR 1 77 T o CNMT Upper Poo l s t....-17 6 T o Equ i pment Dra i ns RX vessel Pool Draindown FR O M FC S U PP LY A Surge Tank B Surge T ank S p e n F u e l S or age Pool l 11 fl ll u J 86B M FLOW D I AGRAM CO N TA I NME N T POOLS TO CO N DE N SER I CNMT BOUNDARY 1 36 FI LL LINE FRO M C Y :~0-1 CY0 1 0 T O FC S U RGE T A NK S 7 FROM FC SUPPLY 157 156 CNMT BOUNDARY RX vessel Pool Fill t f t FRO RHR-_"'----'-

---

, 3B; I I 1 oos I ' ' TO CONDENSER RLLUNE -TO-~ FCSURGE TANKS ocn FC Assist From C P T u 119*' P.oois 1 fe127D A HX RJEL POOL COOLING .N-10 CLEANUP SYSTEM FLO.IV DIAGRA To C Upptf Pock To [IJII nt* _M *-29 RHR PUMP SUCTION Interim Summary 128 FROM UPPER POOLS FC FILTER 023 CAS K TORAGE P O OL A HX B HX SPE T F U B.. POO L FRO M RHR TO UPPER POOLS 30 CY~ Makeup {]J8 RHR -Pump LC Suction 002 001 To Fuel Building Equipment Drain Tank 1R E 01T A Surge Tank B Surge Tank 035 From CNMT Upper Pools 014A 5917-48 Annunciator FC Pump ~-0-----~~*---------

1FC004A 016A 016B FC Pump B 0148 1FC127B FC lter Demineralizer Fuel T r ansfe r P oo l 1FC127D A HX lFCO l AA B HX FCO l AB 1 1 026A From RHR. 0268 FUEL POOL COOLING AND CLEANUP SYSTEM FLOW DIAGRAM To CNM T Upper Pools To Equipment Drains 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 HOLD FD Train Manual Pushbuttons FILTER BACKWASH PRECOAT T abl e s Table l: Table :. Table 3:. Table 4:: Hold Pushbutton Actions and Effects Filter Pushbutton Actions and Effects Backwash Pushbutton Actions and Effects Pree oat Pushbutton Actions and Effects Backwa s h Pu s hbutton Act ion s and Effects 1-1.1s.21 Initiatin g Eve nt Pre ss Backw as h pu s hbu t t o n (PB-3) Act ion B ac k wash l ig ht co m es on, PLC s t a rt s the process. B ackwash program sea l ed in. Sys tem Effects 058 closes FD inl et isolated from FC & SF sys t ems. 068 ope n s Wat er begins to dra in for FD vessel dome. 067 o p e n s S erv i ce Air ad mi tted t o vesse l dome 068 closes Vessel dome is pressurized. 062 c l oses, H o ld Pump stops, 065 FD wa te r & re s in i s fo r ced out th ro u g h o p e n s. ma in d rain. 067 c l oses Serv i ce Air is s hut o ff. 065 closes Vessel drainage stops. 04 1 , 063 & 066 ope n C Y e nt ers t o fi l l FD & flush through ove rfl ow line. 069 opens A i r enters fro m botto m of vessel t o c r eate fr o th in g act i o n & d i s l o d ge resin from septa. (Air Sc o ur) 069 , 063, 066, & 04 1 c l ose 067 o p e n s 06 5 o pens 067 closes 065 closes PL C s t ops th e process, B ackwash li g ht goes o ut , S hutd ow n li g ht co me s on. Vessel fill & sco urin g act i o n sto p s. Serv i ce Ai r pre ss uri zes vesse l dome. FD vesse l water a nd r esi n is fo r ced o ut through main dr a in. Service A ir t o d o m e is s hut off. V esse l drainage s t o p s. 35 Pr eco at Pu s h butt o n Ac ti o n s a nd E ffe c t s (.1.1 5.2 ( l ni1 i: 11 i n g Ev enl Ac ti o n Sys t e m E ff ec ts Pr ess Precoat pushbutton (P B-4) PL C stans the p r ocess Shutdown light goes ou t , Backwash ligh t comes on , and Pr ecoa t pro gra m is sea led i n. B ackwash li g ht goes o ut , Pr ecoa t li ght comes on , and P owe r Failure rel ay i s r ese t (if n ecessary). 063, 066 and 04 1 o pen FD Vesse l fills with CY water. PS-FC024 se n ses hi g h p r e ss u re 066 clo ses Vessel overflow stops. in over n ow lin e 066 opens Vesse l ove rfl ow res um es 04 1 , 063 , and 066 close FD Vessel fill stops Pr ecoa t Pump s tan s 064 a nd 070 o pen 063 opens Clean wate r from Precoat Tank is recirc ul a t ed thr oug h FD Vessel at low now rate. Re si n T imer stans and is sea l ed-in 070 o p e n s to high flo w se ttin g Pr ecoa t r ecirc u l a ti on fl ow rate increases 053 o pen s 060 o pen s S l urry from R es in T an k enters Pr ecoa t Pump suct i on th ro u gh R es in Educ t or Re si n T ime r sta n s a nd R es i n Coating l ig ht co m es o n R esi n s lu rry pump ed 1 0 FD Vesse l w h ere re sin coa t s the FD sep i a fo r 35 minutes 060 cl oses Resin s l urry fl ow is s h u t ofTto Pre co a t P ump s u c tion s tr ea m. 053 closes Resin Coating li ght goes out and Resin Timer rese t s 070 closes t o low fl ow setti n g P recoa 1 rec ircul a t io n fl ow r ate d ec r eases 062 opens and I-f old Pump stans H o l d Pump supp l ies flow through FD Vessel 063 c l oses Pr ecoat P ump supp l y to FD Vessel i s shu1 ofT 064 & 070 c l ose Backwash l ight co me s o n , Pr ecoat li g ht goes o u t , 058 FD inl e t i s l in e d up 1 0 FC or SF syste m ope n s , and Pr ecoat Pump s t o p s Backwash light goes out FD train is n ow in H o l d m ode a nd ca n be p l aced 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 GATE -E r GA TE D STORAGE GATE +-D FUEt CA'S!< S ORAGE POOL GATE C .------, GATE C STORAGE GATE B STORAGE GA T E A STORAGE L RA: F POOL SPENT FUEL STORAGE 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 FCPUMPA RHR LC 004A A HX FROM RHR PUMP 002 SUCTION 001 FCFILTER DEMINERALIZE B HX TO UPPER PCOLS 004 CASK P.:a SPENT TORAGE TRA.',;S."E."!

FUEL POOL "°°'-POOL 41

. Diesel Generator

/Diesel Fuel Oil -

Purpose

• To provide an inde{Jendent, .Onsite source of Emergency Power during Loss of 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 ,-STRAINER FUEL OIL STORAGE TANK Fig 17 DRAIN 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 I_ FUEL OIL TRANSFER PUMP DIESEL GENERATOR 55 PSIG INJECTOR FILTER INJECTOR ASSEMBLY INJECTOR FILTER 0--------FUEL PRESSURE GAUGE (PANEL MOUNTED) MANIFOLD ASSEMBLY i i i i i i '\I I i i i i i i i i FILTER ALARM SWITCH (50 PSI) *-----*--------

r i i ' Fig 18 i _ ........ _ ........ _______________________

_ DUPLEX FILTER FUEL PUMP (ENGINE DRIV!=N) FUEL PRIME PUMP FUEL SUCTION STRAINER TO DAY TANK FROM DAY TANK 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 accelerates 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 AIR (1DG02CA)

RECEIVER s START SIGNAL 1DG640 CYL TANK (1DG644) EN 1DG04TA 1DG16ML(N)

(1DG05TA) 1DG( GOVERNOR BOOST AIR MOTOR 1DG012D(H)

AIR MOTOR *I AIR 1DG16MA(E)

DRYER 275 PSIG s START SIGNAL 1DG638 1DG21DA(B)

(1DG642) 1DG012C(G) 1DG16MB(F) 1DG012A{E)

GOVERNOR BOOST AIR MOTOR AIR AIR MOTOR CYL RECEIVER 1DG008B(F)

OILER TANK 1DG646B(F) 1DG16MM(P)

EN 1DG94TB s START SIGNAL 1DG639 1DG( AIR (1DG05TB)

(1DG643) COMPRESSOR 1DG01CB 1DG011A(C)

(1DG02CB)

GOVERNOR BOOST 1DG16MD(H)

AIR. Fig 18 1DG008D(H)

MOTOR OILER 1DG6.46D(H) . 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 *I DRYER 250 PSIG 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 PISTON -COOLING-I Fig 20 ===----======, I TURBO OIL PUMP 480 VAC TO TURBO , I TURBO []FILTER J 125psi CIRCULATING OIL PUMP 480 VAC V TURBO SOAK BACK PUMP 125 voe 75 PSI Cl;CULATING t OIL PUMP I l l 125 voe STRAINERO ENGINE SUMP 30-40ps i d LUBE OIL FILTER SCAVENGING PUMP FILTER BYPASS RELIEF VALVE 4 o psi SETPOINT LUBE OIL COOLER TO MAIN BEARING HEADER ENGINE WATER __ _ OVERFLOW STRAINER SUMP IMMERSION HEATER STRAINER MAIN LUBE AND PISTON COOLING PUMPS Fig 8 Oit From Engine Sump Piston Cooling Oil Oil To Bearings Main Lube Oil And Piston Cooling Oil Pumps Vent To Engine -===-=== . ---1 Cooling Wate Lube Oil Circulating Pump ~ections Lube Oil l Cooler . 1 Auxiliary Turbocharger Lube Oil Filter 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

• Header Temp gages on accessory of DG 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"

• Provides oil to turbocharger when DG shutdown

• AC and DC backup

• 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

RSP TRANSFER SW. EMERGENCY MCR START SELECT SW. DIESEL ROOM MCR CONTROL SW. START MCR START SELECT SW. CONTROL ROOM LOCAL ENGINE START SW. START LOCA RSP r----TRANS FER SW. -~ START NORMAL AUTO START CIRCUIT 86 LOCKOUT RELAY LOCAL ENGINE MAINTENANCE SW. MCR CONTROL SW. AUTO LOOP

• +-' C 0 u en +-' L. co +-' en 0 +-' :::s <( RSP TRANSFER SW. EMERGENCY MCR START SELECT SW. DIESEL ROOM MCR CONTROL SW. S1ART MCR START SELECT SW. CONTROL ROOM LOCAL ENGINE START SW. START LOCA RSP ,----TRANSFER SW. START NORMAL AUTO START CIRCUIT 86 LOCKOUT RELAY LOCAL ENGINE MA IN TENANCE SW. MCR CONTROL SW. AUTO LOOP DG Trips

• Engine Overspeed

• 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 Overspeed

• 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 -Engine Overspeed

-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 (Div 1 & 2) -Differential Overcurrent

• Auto Starts -Division I & 11

• High Drywell Pressure (1.68 psig) and/or

• Low RPV Water Level 1 (-145.5")

• Bus Undervoltage

-b. Division 111

• High Drywell Pressure (1.68 psig) and/or

• Low RPV Water Level 2 (-45.5")

• Bus Undervoltage 81

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 w i th: DG Rm lA(B) [C] Vent Fans , 1VD01CA(B)

[CJ in STANDBY. DG Vent O i l Room lA(B) [C J E xh 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 PF AINA OD 1 ES8L G EN E RA OR ROO?, 1 C OD 1 E S 8L G BN E RATOR ROO' 1 A DIESEL , GE -RATOR R 1 0 1 0 AK UP SYSTE. HVAC ODI E S E G E ERA TOR ROOM 1B 1V D 01Y A DIESEL 1 G RAT0 1 R V TSYS EXHAUST FA DlESELG I EINERATO I R IROO 1A (1B ,1 C) IOAY TANK ROO M I 1A (1B , 1C) 1V010Y A(B,C) IET L 1V D 08Y A (B , C) OL TANKROOIM 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 1 VDO 1 YA(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.

(MCR) Sar* DG Rm lA (B) [C J Vent Fa ,. 1VD 0 1CA(B ,) [C J ..

3. I ncreasin g Cooling/PURGE Mode 3403.01, Section 8.3 (Cont.) ( oca) i e -) ) IF desired fo r te perat re/PURGE co t r o l , T HEN pace D i v 1(2) [3] rge Switch to URGE. v 1 3] at entrance to *v 1 3] DG Roo, v a CB , 755' H VAC Mezza 1 i ne , Y-129.) 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 Sw i 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 1 A(B )[C] Room Vent Fan, 1 VDO 1 CA(B )[C]

• DG Vent Oil Room 1A(B)[C] Exh Fan, 1VD02CA(B)[C]

• DG Make-Up Fan A(B), 1 VD03CA(B)

• Makeup Fan Discharge Damper, 1 VD25YA(B)

• Filter Isolation Damper, 1VD18Y

• Exhaust Damper, 1 VD03YA(B)[C]

• Back Draft Damper, 1 VD27YA(B)[C]

• Fire Dampers 1 VD08YA(B)[C]

& 1 VD1 OYA(B)[C]

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

1 . CO2 Initiation 3403.01, Section 8.8 (Cont.) .hen th ~02 I niti ti 1) Purg* A (B) '"' ) . L.. a f , -e Ma . t e t J-_e f 1 1 0 .... A ')lV O .. :fB 3 1 _.Q Y *1*J10 .. :fA 1 lOYB 1 _.10 .. :f C a ce . l I sig [ J p r e a e e a ) ~t rt V per s tin *.1. l .1. s ti t. e f* e -"' "' r ._. :

• 3 . e ,

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 41N.--QIN.--FLOAT CHAMBER FULCRUM ---WATER /J\~41N. //\\VALVE IN --WATER OUT 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 a. To compare and discuss flow 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

• Equal Percentage 3: 0 ...J u. 0 100 % 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 Because of large volume of pneumatics required to operate valve , valve positioner has independent, regulated, pneumatic supply. 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) 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)

Request: Training be performed for E0-1 and EO-C populations on 1 PA05J controller operations.

Newer equipment operators do not have full understanding of how to operate Bailey/NUS controllers at the 1 PA05J panel in a transient condition.

MOVABLE SETPOINT / MEASURED VARIABLE INDICATOR SCALE MEASURED VARIABLE/

ERROR POINTER OUTPUT POINTER MANUAL INDICATING LIGHT e MANUAL BUTTON --=60 -=-so ----SETPOINT THUMBWHEEL FIXED SETPOINT HAIRLINE OUTPUT SIGNAL METER MANUAL ~~PUSHBUTTON e AUTOMATIC BUTTON (Increase Output) AUTOMATIC INDICATING LIGHT 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 1 ' ,, \ ,' ,, HP TURBINE 4 ,, / 6 SS E (LP TURB) " A" ONL Y For the mathematically i nclined: 1 + 4 + 6 = 11 1 0 + 2 = 1 2 6 + 5 = 11 1 2 + 1 = 1 3 7 + 4 = 11 7 t h G r ade rs ate 7 8 LP TUREINE S ten dozen don u ts 1 Q 12 (TUREINE EXTRXTICN ST .llGES) G ENERATOR 1 2 CB PUMP S ,---'---, R E CO MB S J A E S PE C D PUMP S 8 + 3 = 11 C O 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)

FROM HPTURB EXHAUST TOMSR FROM LP TURB lB 7TH STAGE .AO lESOl6A .AO lESOBA TO .__--~----~CONDENSER .AO lESOlcSA AO 1ES033A MO 1ES009A TO '1:....---1

_... ____________

..,.CONDENSER HPHEATER 6A LP HEATER SA LP HEATER 4A 109 Flowpaths cont. Extraction Steam Startup / Abnormal Operation (One Heater String Shown) (fig. 3) EXTRACTION STEAM SOURCES FROM HPTURB 4THSTAGE (AND 1ST STAGE DRAINS) FROM HP TURB EXHAUST TOMSR FROM LP TURB lB 7TH STAGE AO 1ES026A AO lESOBA AO TO 1----C> CONDENSER lES016A TO CONDENSER AO 1ES033A MO 1ES009A TO t----------------------c:=--

coNDENSER HPHEATER 6A LPHEATER 5A LPHEATER 4A 110 Flowpaths cont. Heater Drains Normal Operation (One Heater String Shown) (fig. 4) Con de n se r Con de n ser Con de n se r Con de n se r Con de n se r Con de n se r .. 111 Flowpaths cont. Emergency Drains (fig. s) REH EA TER DRA I N TANK I A -----**-*****-**

• -.. ------i P....------;-,.-

-;:::,,<: 1--~ TO CONDENS~R LP HE ATER I A ,-**-**-***-***-***-

-**-**-**-***-***-***-***-**-~ I ! I

• I I L.._+-l : ............... : TO : CONDENSER! TO CONDENSE R TO CONDENSER TO CO DE SER TO CON D ENSER 112 Components Feedwater Heaters EA T ER DRA IN OOOLER STAR T-U P VE T CONDENSATE OUT CONDENSATE.

I N DRA I INS O U T EATER OPERAT IN G V E NT MA IN CO N DENSER H EATER ---------.

START-U P --V ENT BAFFLE SUB-COOLED DRAINS HOT DRAINS I N I ATERS 2 6 D I IV I DER PLA T E 113 Components cont. Flash Tanks 2A/B ES c s---~...-...........

LP Heat 1A/B 114 CONDENSATE OUT Components cont. Drain Coolers DRAINS IN CONDENSATE

__ _._ OUT DRAINS IN CONDENSATE IN DRAINS OUT --------------------------------------------------

CONDENSATE DRAINS DIVIDER PLATE IN OUT 115 Components cont. Extraction Steam Isolation Valves FROM HPTURB 4 TII'S T AGE (AND lST'SI'AGE DRAI N S) AO 10 I--...... CONDENSER HPH EA'IE R 6A 116 Components cont. Extraction Steam Check Valves FROM LP TURB I B 101H STAGE FROM LP TURB IB 101HSTAGE 0 TO CONDENSER SHAFT CYLINDER PISTON ROD SPRING PULL DOWN BOLT 117 Components cont. Heater and Drain Cooler Normal Drain Valves Normal Drain Valves Fail CLOSED on loss of air or power Auto CLOSE on high level in downstream heater Emergency Drain Valves Fail OPEN on loss of air or power Auto OPEN on high level in associated heater 118 Components cont. Heater and Drain Cooler Emergency Drain Valves Normal Drain Valves Fail CLOSED on loss of air or power Auto CLOSE on high level in downstream heater Emergency Drain Valves Fail OPEN on loss of air or power Auto OPEN on high level in associated heater 119 Automatic Functions/

Interlocks

• High Heater Level

• High-High Heater Level

• Main Turbine Trip 120 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 310201.16 Respond to. Feedwater Heater Abnormal Level 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 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. Highfeedwater heater levels cause extraction steam valves to the respective heater to close. If this occurs, refer to CPS 4005. 01, Loss of Feedwater Heating while continuing in this procedure.

NOTE See Appendix B, HEATER VALVE LIST for valve numbers associated with each heater vessel. Emergency drain valve controller output is" 100%for valve fully closed. 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 Respond to Feedwater Heater Abnormal Level cont. 8.3.1 Feedwater Heater Abnormal Level (cont'd) 2. IF Feedwater Heater Abnormal Level is result of a plant manipulation 9r transient (i.e., bypass valve operation, removal/ restoration of FW Htrs, etc.) , <<CM-6>> THEN After stabilization of the feedwater heaters, verify proper operation of the feedwater heaters: 1) Normal level being maintained. (P680/1PA05J).

2) Normal and Emergency Drain Controllers operating properly.

3) ES isolation valves positioned correctly.

4) 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 310201.19 Preparing Feedwater Heater Level Control For Maintenance Or Trouble-Shooting Of A Normal Drain Valve Malfunction CAUTION Section 8.2.3.1 shall be reviewed prior to proceeding due to changes infeedwater heating. 8. 3. 4 Preparing Feedwater Heater Level Control For Maintenance Or Trouble-Shooting Of A Normal Drain Valve Malfunction

1. At panel 1PA05J, verify level indicating cont.roller for the emergency level control valve is in AUTO, and controlling at a reduced setpoint as described in 8.3.1.1.3.*

2. Verify/place the normal drain*controller in MANUAL. 3. Slowly close the normal drain valve using the closed push button on the level indicating controller while observing that the emergency level controller responds to maintain heater level. 4. IF Necessary due to the malfunction, THEN 1) Isolate the malfunctioning drain valve. (refer to Appendix B Table 1 for list of normal drain isolation valves) 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 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 B. C. D. TOPIC lmRODUCTION

.. ..................................... . . OVERVIEW OF TRAINING SESSION ............. . EVALUATION

• ..*.*....*..*..*..*.............*..*.............*...

MANAGEMENT E.XPECTATIONS

......*.....*.............

.............

1 .. .....................

2 ...2 . .........

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.)

Figures 129 Attachment 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 ,C "* c. D. II. 1YSTE..'I PURPOSFJIJF.<;IGN IIASIS .... -.... ----**-****

...........................

---

***---******-********-*****---* ,I A. SYSTEMl'URPOsE................................

• • • • • • • • ---***-

...............

,1 H. DESIGNflASIS

..... , ... -... .. ..............................................................

-...............................................................

,1 III. .!.'\'STEI\.IFLO\\'l',\Tll{S).....................

.. ............................................................................

.. ;. ~::~*,;v;f~i::~iii~;;;;:;;;;~::;~:;;;:;:i;~::::::::::::::::::::::=::::::::::::

l c. R~o; ~=-}::;;;;;~~;;;=::::::=.=.=.:

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H *;J II. C. D. E. I'. V. INTERLOCKS Cl Copyright 2007 by Exi:lon Nu,;kar, ,\1111.ight*

Reserved.

Fmnission for rq,mduction and use i* reserved for Exelon Nuckar, {Anyo1hcruscnrn.ymductionisc:1pn:~.tvpruhibited"i!hnutthecxpn:sspcrmii,.,ionoffac]nnNuc],:ar.J 130 Phase Separators

-3909.02 D 1 iscussion The Phase S~parators collect waste sludge from the Reactor . ~'Jater Clean Up Fi 1 ter Demineralizer 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 recirculation 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 I Phase Separator Lvl Reading 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. 132 ' i ' i

8.6.3 Phase

Separator Lvl Reading (Cont.) 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 of settle 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#.

!

I I I 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)

.. , No. L 5. A fifth sequence gives QUANTITY OF CHANNEL# (gallons/cu.

ft.). OF SEQUENCE READOUT 1 Feet 2 Alarm 3 Material 96 4 Feet 5 Gallons/ Cu. Ft. J I CPS 3909.02 ,I I! 8. 21 Resetting a Locked Up Quantum Master Controller 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 8.21.2 8.21.3 8.21.4 ':8.21.5 L_ Obtain SMngt authorization to reset the locked up Quantum. Master Controller.

• open the Quantum Master Controller cabinet on OPL08J. 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. Re-install the 5 amp fuse removed in the previous step, 8.21.3. 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 Get Liquid Depth Decant Line ' ; Get Sludge Depth I H o m e OWX04T Ill Last Sludge MeasureMent 1 1r<<-1~1 1a~=1*1 l!D-5 .38 Feet I! LIQUID & SLUDGE MEASUREMENTS CANNOT BE TAKEN SIMULTANEUOSLY 139 140 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 8.18.2 8.18.3 8.18.4 Obtain Shift Management authorization to reset *1ocked up 0LIX-WX513, WX Level Control PLC. Open the back panel door on OPLOBJ to obtain access to the back side of OLIX-WX513, WX Level c*ontrol PLC. Use the proper electrical safety precautions per SA-AA-12 9, Electrical Safety, for the folln-;;11,ring steps. 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 8.18.6 8.18.7 8.18.8 Remove the green 3-position power terminal block connector by pulling down on the connector until it is removed from the controller.

Wait a minimum of 10 seconds before proceeding.

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

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

• Anion underlay --20 barrels A-284-LS (1 OOcf).

• Mixed bed portion * -11 barrels cation C-471 (55cf) and 8 barrels anion A-284C 144 Loaded

• Anion underlay loa*ded -4 barrels A-284C (20cf) and 16 barrels A-284-LS (80cf)

• Mixed bed portion loaded. -11 barrels cation C-471 (55cf) -4 barrels anion A-284C -4 barrels A-284-LS WASTE DEMINERALIZER Figure 2 WATER INLET / V!lffllll!ll#llll!l#/1&$ff/,l@#I/Effl1 INTERMIXED CATION W!lll!lllliWll!#f§l$t1f'm11!11,f/JJ1 AND ANION RESIN UPPER DISTRIBUTOR REGENERANT DISTRIBUTOR INTERFACE COLLECTOR UNDERDRAIN ASSEMBLY FALSE BOTTOM WATER OUTLET 145 ischarge

• 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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_, --*--! -*...u. ,_,tttl -~ I I 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} Lesson ID: N-CL-EOC-1701 Exelon Generation 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 233000.1.1

-STATE the purposes of the Fuel Pool Cooling & Cleanup System including applicable design bases. 233000.1.2

-Describe the major flow paths for the following modes of the FC system .1 Normal _Flow path .2 RX vessel pool draindown

.3 RX vessel pool fill .4 FC assist .5 Alt Suppression pool cooling 233000.1.6

-Given a Fuel Pool Cooling& Cleanup System Annunciator, DESCRIBE:

b. Any automatic actions 233000.1.7

-Given the Fuel Pool Cooling & Cleanup system, DESCRIBE the 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 Slide(s) 20-22 23-29 31 32 33-36 Lesson Title: 2017 Cycle 1 Training {DG-DO, ES~HD, FC, RW, VD, TREQs, Mods & LL} Lesson ID: N-CL-EOC-1701 Objectives Using the approved procedure, DISCUSS: Task 331701.18

-Lower FC Surge Tank Level During System Operation Exelon Generation Slide(s) 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) 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 264000.1.1

-STATE the purpose(s) of the DG/DO System including applicable design bases. 264000.1.2

-Describe the major flow paths for the following modes of the DG/DO 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 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 the nature of the support . . 1 DG Auto Starts Slide(s) 43-44 45-4 7, 52-66 48-51 74-75 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 264000.1.11

-EVALUATE given key DG/DO System parameters, if needed 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 Slide(s) 76-77 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 the approved procedure, DISCUSS: Task Description Task 350601.17

-Diesel Engine Lube Oil Addition or Removal Task 350601.27

-Respond to DG 1A(18)[1 CJ Auto Start Task 350601.34D

-Alternate Diesel Generator Start -Manual Override of Air Start Solenoids Slide(s) 78 79 80 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, (he trainee shall: Objective Description 233000.1.1

-STATE the purpose(s) of the DG ROOMS .HVAC System including applicable design bases. 233000.1.2

-Describe the major flow paths for the following modes of the DG ROOMS HVAC system operation . . 1_ Normal Standby Mode .2 Diesel Generator Operating Mode .3 Purge Mode Slide(s) 83-84 85-87 Lesson Title: 2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Lesson ID: N-CL-EOC-1701 Objectives Using the approved procedure, DISCUSS: Task Description Task 340301.03

-Increased Cooling/PURGE Mode of the VD System Exelon Generation Task 340301.08

-Respond to a CO2 Initiation with respect to the VD System Slide(s) 88-90 91-92 Lesson Title: 2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, Mods & LL) Lessor:, ID: N-CL-EOC-1701 Objectives Exelon Generation 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 BC081r4_Controllers

4. State the purpose of a controller.

'--BC081r4_ Controllers

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

a. Two position b. Proportional

c. Proportional-plus-reset (Pl) d. Proportional-plus-reset-plus-rate Slide(s) 96 97-101

• 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 1 PAOSJ. 105 *-

Lesson Title: 2017 Cycle 1 Training (DG-DO, ES-HD, FC, RW, VD, TREQs, M0ds & LL) Lesson ID: N-CL-EOC-1701 Exelon Generation 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) Lesson ID: N-CL-EOC-1701 Exelon Generation 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 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 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):

.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 Task 310201.19 Preparing Feedwater Heater Level Control For Maintenance Or Trouble-Shooting Of A Normal Drain Valve Malfunction Slide(s} 120 121-122 123-124 125 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 re_ferences, unless otherwise stated, and with 100% accuracy, in accordance with course reference materials and pro~edures, the trainee shall: Objective Description 268013.1.1-ST A TE the purposes of Spent Resin System 268016.1.4-STATE the physical location and function of the following SOLID RADWASTE SLUDGE COLLECTION/DISPOSAL system controls, indicators, and/or sensors . . 9 Quantum Master Control Console .10 Tank Level Instrumentation 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. [ Slide(s) 138 127-130 145 /

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 the approved procedure, DISCUSS: Task 390901.02

-Spent Resin Tank-level readings, 17 Resetting a Locked Up Quantum Master Controller Task 390902.06

-Phase Separators Level Readings Task 390903.02

-Waste Sludge Tanks level readings Task 390904.03

-Concentrated Waste Tanks level readings Task 390905.02

-FP/FD Sludge Tanks level readings TREQ 02623308-33

-Liquid RW Discharge Surveillance TREQ 02623308-21

-Resin Loading activities TREQ 02623308-01

-WX Tank Level Mod Slide(s] 141-142 131-137 137 137 137 146 143-144 139-141 Questions 160 Feedback Feedback is essential for program health LASER entries provide anecdotal measures of effectiveness , . Training Observations are accessed from the Exelon Intranet -Exelon: atea11 swa11tto ::i Lenders At Odds Over th Forward 1ders say they llave vith tile company's udgetfor, In the ... -**, -...-1--. I l!!ll!ll!ll I' t;luclear,O~g

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161