Startup / Shutdown Flashcards
- During a reactor startup why do we commence shell warming at 60 psig?
To reduce the potential for the Turbine to roll off the Turning Gear, shell warming should begin as close to 60 psig Reactor pressure as possible.
OP-21 P&L-13
- With shell warming in progress the procedure provides guidance for removing turbine lift pumps. Why would we need to remove lift pumps from service and how many total can be removed from service during turbine shell warming?
Remove pumps from service to prevent turbine from rolling off the turning gear. Should not exceed 50RPM. May shutdown 6 of 8 lift pumps, must maintain lift pumps for bearings 9 and 10 (P6G/H - Generator Bearings) running.
OP-21 page 22
- While performing a turbine startup, OP-21 provides directions to trip the turbine under certain turbine conditions. In addition to listing the requirements for tripping the turbine on vibration, list 3 other items that require a turbine trip during startup in accordance with OP-21?
~CAUTION~
If water induction is evident while Turbine is accelerating, Turbine must immediately be tripped and placed on turning gear to prevent or minimize damage to the Main Turbine.
IF any of the following occur WHILE bringing the Turbine to speed, THEN immediately trip Turbine per N2 SOP 21, Turbine Trip [C4].
• Signs of water induction into Main Turbine
~NOTE~
Turbine Bearing Vibration indications shall be confirmed using adjacent bearing(s) indication, bearing temperature indication, (etc. 2CEC-PNL842 and computer points indications) or local investigation.
• Any confirmed Turbine Bearing Vibration greater than 9 mils with greater than 3 mils/minute rate of change
• IF any confirmed Bearing Vibration is greater than or equal to 12 mils WITH two consecutive readings on recorder 2TMI NBR134.
• Any confirmed Turbine Bearing Vibration greater than or equal to 10 mils for 15 minutes
• Smoke OR fire associated with Main Turbine OR Generator/Exciter
• Other unusual conditions as directed by SM/CRS
OP-21 E.5.15
- What is the heatup rate limit when warming up the cross around piping during shell warming?
To reduce metal thermal stresses and potential rubbing due to uneven component expansions during activities such as shell warming and changes in load, High Pressure Turbine Shell Temperature changes should have a target rate of less than 125°F/Hr and are limited to a rate of 150°F/Hr, or about 40°F every 15 minutes.
P&L 22
- When is chest warming required to be performed during a turbine startup?
~NOTE~
Chest warming is required if Control Valve Inner Temperature is less than 500°F (Computer Point TMITA02 or Recorder 2TMI TR137/ZDR135, Point 6).
OP-21 E.4
- What is the high pressure turbine shell temperature requirement to support startup of the turbine?
OP-21 E.5.3.2 High Pressure Turbine Shell Inner Temperature is greater than 250°F.
- During turbine rollup to rated speed at what speed range would you expect to experience the highest vibration levels?
~NOTE~
• Personnel performing this procedure should be familiar with expected Turbine startup vibration. Vibration should peak during Rotor Critical Speeds (about 900 to 1300 rpm).
• No automatic turbine trip exists on high vibration.
OP-21 above E.5.4
- SRO Only – While preparing to take the mode switch to startup OP-101A requires verification of all Mode 2 surveillance requirements being up to date, list 4 things that you would check to ensure that Mode 2 surveillance were current?
- CR Logs
- ESL
- Clearance Module
- PMST
- NewCap
iaw The Scag
- At what point in the reactor startup are we required to go to single notch withdrawal of control rods? (List at least 4)
Single notch control rod movement shall be performed from notch positions 00 to 36: [C19]
− At the direction of the Reactor Engineer if Estimated Critical Range (ECR) is PRIOR to Rod Worth Minimizer (RWM) rod group 3.
− IF 3 count rate doublings are approached on at least 2 SRMs PRIOR to RWM rod group 3.
− Starting with RWM rod group 3 UNTIL criticality is achieved.
− For RWM rod groups 3 AND 4 AFTER the reactor is critical, unless otherwise directed by Reactor Engineer.
OP-101A att 1.D.1
- Match the approximate rod worth to the list rod position.
a. 00-04
b. 04-08
c. 08-12
d. 12-16
e. 16-24
f. 24-48
- Highest
- Low
- Minimal
- High
Position Worth
00-04 Low 04-08 High 08-12 Highest 12-16 High 16-24 Low 24-48 Minimal
OP-101A att 1.D.2
- Who is responsible to determine what systems will be required to have valve / electrical lineups performed on prior to performing a plant startup?
The General Supervisor Operations (or designee) shall identify those systems for which a system lineup is NOT required. This decision will be based on the extent of work performed on the system during the outage and the safety significance of the system.
OP-101A Att 3
- What are the requirements for performing rod exercising prior to startup if the shutdown was the result of a reactor scram?
- Insert Flush until Stall Flow Stabilizes.
- Continuous Withdraw to 48*
- Withdraw Flush Until Stall Flow Stabilizes
- Full Stroke Time Any Rods with Insert Stall Flows > 3.5 gpm and adjust fast control rods Estimated Time = 30-36 hours
OP-AB-300-1005 Attachment 2
- How many days prior to startup should the Off-Gas Recombiner heat trace be placed in service?
Commence Off Gas recombiner heat trace warming per N2 OP 42 at least three days PRIOR to planned start up of Off Gas System.
OP-101A Attachment 3.D.5
- SRO – A plant startup is in progress following an outage which required work on the Reactor Core Isolation Cooling System. Per the startup schedule N2-OSP-ICS-Q@002 is a required PMT for the work performed. When during the startup does the 12 hour clock start to complete the surveillance test?
Can NOT exceed 150psig before performing N2 OSP ICS Q@002 for SR3.5.3.4 (OP-101A E.2.37)
~NOTE~
When reactor pressure exceeds 935 psig with 1 turbine bypass valve full open and N2 OSP ICS Q@002 is required, a 12 hour clock for test performance will start. (SR 3.5.3.3)
OP-101A above E.3.18
- During power ascension we place condensate demineralizers in service as needed to maintain condensate demineralizer flow between what values?
~NOTE~
Eight demineralizers are required for 100% power. Nine demineralizers are preferred for additional operational margin.
Place Condensate Demineralizers in service as required in order recommended by Chemistry AND maintain individual demineralizer flows between 2000 AND 3300 gpm (3500gpm MAX) AND a system delta P less than or equal to 55 psid (60 psid maximum).
OP-101A E.5.4
- SRO – Reactor Power exceeded 23% at 1300 today, when must the Jet Pump Operability surveillance test be completed by?
Within 24 hours AFTER exceeding 23% of RATED THERMAL POWER, perform N2 OSP LOG D001, Daily Checks, Jet Pump Operability. (TS 3.4.3)
OP-101A E.5.9.3
- Why do we transfer Feedwater Level Control to Single Element at ~ 25% power during a plant shutdown?
~Caution~
It is possible, following RCS pump downshift, that steam flow indication can drop low enough to cause difficulty with 3-element feedwater level control. Should this occur, G.1.26.1, “Placing feedwater level control in single element,” should be performed without delay following the downshift.
N2-OP-101C Section G (pg. 18 of 92)
- Why are 3 Heater Drain Pumps required to reach full power?
HDL Pumps provide 1/3 of total condensate flow – may have trouble maintaining RPV Level at 100% without challenging the Condensate System with Runout.
Additionally iaw P&L 17 of OP-8, long term operation on the high level dumps could cause condenser damage.
- What actions are available to support control of reactor water level if the Feedwater LV10’s are suspected of having leakby?
~CAUTION~
Seat leakage problems have been experienced with the 2FWS LV10s in the past. After valve repair, the leakage is eradicated or minimized but will degrade as the valve wears. If leakage past the LV10s has been observed to be degrading, caution needs to be observed when opening 2FWS MOV47A, B, C valves. Leakage past the LV10s can cause level and associated power excursions, particularly at lower reactor pressures. [C3]
IF 2FWS LV10A(B) leak by is suspected,
THEN make 2FWS MOV47A(B) throttleable per H.3.0 of this procedure.
OP-3 E.3.43.1
- During a plant shutdown by individual control rod insertion a pressure control malfunction requires the use of SRVs to maintain the ordered pressure band, what actions are required by procedure for control of the reactor?
IF SRV opening is required to control rising Reactor Pressure, THEN exit this procedure AND enter N2 SOP 101C, Reactor Scram.
OP-101C G.4.19
- What portion of the reactor startup do we implement controls for Infrequently Performed Test or Evolutions? List 5 things that we do to manage the risk during the IPTE?
WHEN Reactor pressure reaches approximately 925 psig, THEN perform the following:
IPTE portion of plant startup is now complete. Log completion in Control Room Log.
OP-101A E.2.49
- While performing actions in SOP-101C pressure control leg, you are taking action to place the Mechanical Vacuum Pumps in service. How do you verify that there are no indications of fuel failure prior to starting the vacuum pumps?
Verify Main Steam Line Hi-Hi Rad Alarms are Clear
SOP-101C Discussion 5.8
- While preparing to commence a plant startup, why must we secure shutdown cooling before we can place the mode switch to startup and enter Mode 2?
Residual Heat Removal System removed from Shutdown Cooling mode AND operable for LPCI mode per N2 OP 31, Residual Heat Removal System
OP-101A E.1.16.1
All ECCS Must be Operable prior to Mode 2 Entry iaw Tech Spec
Additionally, you do not want anything other than Rods affecting reactivity during startup.
- While performing a reactor startup and heatup, drywell pressure rises to .5 psig. Describe the potential impact on inerting the containment and any required actions?
To prevent crossflow from the primary containment to the reactor building when using the 20” line to GTS, (2GTS*AOV101), the following plant parameters shall be maintained:
i. Primary containment pressure less than 0.41 psig.
ii. Reactor building pressure shall not be more negative than −1.0” water.
iii. Purge flow (air/nitrogen) shall be maintained less than GTS out flow.
OP-61A P&L 7