Exam 3 Flashcards
(36 cards)
SLIS
- Signals
- What happens on SLIS?
SLIS
- 615 psig (2/3 PTs on 1/4 S/Gs)
- 100 psid drop in 50 sec when < P-11 w/ low Pstm SI blocked (2/3 PTs on 1/4 SG/s)
- CTMT Hi-2 (17 psig on 2/3)
Closes
- MSIVs
- MSIVBVs
- Low Point Drain IVs
- TDAFP Warmup Valves
SGBSIS (Steam Generator Blowdown Sample Isolation Signal
- Causes
- Valves Closed
Causes (SUM)
- SI
- UV on NB01 or NB02
- MDAFAS
Valves Closed
- BD Isolation Valves: BM-HV-01 thru 04
- Sample Isolation Valves:
- BM-HV-35 thru 38 (Lower)
- BM-HV-19 thru 22 (Upper)
- Outer Sample CIS Valves: BM-HV-65 thru 68
Main Feed Pump Speed Controller
- Operation in following modes:
- Auto
- Manual
- Valve Control
- Overspeed
Auto
- Controls steam admission valves based on speed demand
- Setpoint comes from master controller
- Low Stop - 3650 rpm
- High Stop - 5712 rpm
Manual
- Controls speed setpoint input by operator
- Controls from 0-5712 rpm (no low speed stop)
Valve Control
- Operator contols steam admission vale position (%)
- No speed feedback
Overspeed
- Speed demand set using arrows.
- Controls from 0-6225 rpm (no low speed stop)
Aux Steam Loads
- Steam Seal System
- MSR Tube Blankets
- Plant Heating
- Various Storage Tank Heating
- Main Condenser Sparging
- Decontamination System
- Aux Feed Pump Turbine (TDAFP)
- Main Turbine Shell Warming
- Laundry Dryers
Main Feed Annunciators
- MFP suction pressure low
- Bearing oil strainer DP
- MFT/MFP oil pressure low
- ACC Tank N2 pressure low
- MFP LO Cooler Temp Hi
- MFT Turbine Bearing Hi Oil Temp
- Setpoint: 325 psig. Suction pressure must be > 240 psig for 2 MFPs, > 300 psig for 1 MFP.
- 15 psig
- 5.5 psig
- TKA02-TKA05: 625 psig, TKA06: 450 psig
- 135°F
- 180°F
Heater Drain Tank & Pumps
- Inputs to Tank
- Pump Flow
- Pump Cooling
- Motor Cooling
- Recirc Valve Operation
- Trips
Inputs
- # 5 Heaters
- # 6 Heaters
- MSDTs (Normal)
- SGBD Flash Tank Vent
- SGBD RHX Condensate Outlet
- Reboiler Drain Tank
- HDP Recircs
- SUFP Recircs
Pump
- 50% flow
- Pump cooled by flow
- Motor cooled by Closed Cooling Water (CLCW)
- Recirc valve opens @ < 1250 gpm
- Fails open on loss of air
- ‘A’ trips on Low-Low Level (5” from bottom of sightglass)
- ‘B’ Trips on Low Level (17” from bottom of sightglass)
Main Feed Water System Bypass Switches
- S701 on SB029D/SB032D
- FC HIS-82/182 on RP068
- FC HS-25/26 on RL028
- Bypasses P-4/564 FWIS to prevent actuation when opening RTBs during normal shutdown.
- MFP A/B FWIS trip block: Permits emergency start of MFPs during FR-H.1 (EOP Add 30 & 31)
- AFP ESFAS Train A/B Block - prevents inadvertant AFAS when tripping both MFPs in Mode 3 during normal shutdown.
CST
- CST Volume & Basis (T/S 3.7.6 Requirements)
- Connections to pumps/systems
- CST temperature band & heat trace supply
HCST
- Purpose, Size & Mission Time
- Swap-over setpoint
- Temperature control
CST
-
CST Volume & Basis (T/S 3.7.6 Requirements)
- __450,000 gallons
- Insulated & vented
- Has floating cover & N2 purge to minimize O2 intrustion.
- 281,000 gal T/S requirement.
- Applicable in MODES 1-3
- (~60%) allows 4 hours in HSBY and 4 hours to Cooldown to RHR entry conditions.
- Includes volume to prevent ESW swap over and minimum AFP NPSH.
-
Connections to pumps/systems
- __Suction to AFPs, NSAFPs, AFP Mini-Flow returns, makeup & reject, NSAFP Recirc return (via reject), Condenser Vacuum Pumps, seal water makeup, Demin makeup, N2, overflow to LSW.
-
CST temperature band & heat trace supply
- __55-70°F
- Heat trace maintained by Aux Steam
- Makeup 85-89%
HCST
-
Purpose, Size & Mission Time
- __450,000 gal, enough to supply AFPs after loss of CST & ESW for 30-36 hours.
-
Swap-over setpoint
- __1/2 at 11.5 psig AFPs suction auto swaps to HCST
-
Temperature control
- __Maintained > 50°F by submersible heaters
ASDs
- Lift Setting
- Flowrate & MS System Rated Flow
- Operation Locations (Controllers & Manual)
- 1125 - 1185 psig
- 594,000 lbm/hr, ~3.7% per valve, total MS Flow 16x106 lbm/hr
- MCB or ASP.
- Transfer switch on ASP
- B&C ASDs have local controllers in Area 5
- All ASDs may be operated with handwheel.
BSPIS
(Blowdown Sample Process Isolation Signal)
- Causes
- Valves Closed
Causes (BSPIS Sounds like Urinae, Closed Valves 1 thru 8)
- Blowdown Process Surge Tank Hi Level
- Blowdown Flash Tank Hi Level
Valves
- BD isolates BM-HV-01 thru 04
- Outer Sample CIS Valves BM-HV-05 thru 08
Feed Pump Master Controller
- Operation in Auto-High Power & Low Power
- Operation in Manual
- How to transfer between MFRV & MFRBVs, Timing, and how to cancel
Auto
- High - Controls D/P on progam
- D/P is difference between Median Feed Pressure (AE-PT-0508A/B/C) vs. Median Steam Pressure (AB-PT-507A/B/C).
- Steam Flow is sum of 4 loops averaged density compensated steam flow.
- Low - Maintains D/P at 215 psid, arrows control setpoint.
- Used when using MFRBVs, which requires a fixed D/P
Manual
- Up/Down arrows control MFP Speed deman to adjust D/P
How to Transfer, Timing, and Cancelling:
- To Transfer, hit Xfer button as appropriate provided permissives are met.
- Starts 720 second cycle timer
- To cancel, hold manual on valve controller for 3 seconds until manual button lit & not blinking.
Aux Boiler
- Power Supplies to:
- Forced Draft Fan
- Fuel Oil Booster Pumps
- Aux Steam FW Pumps
- Major & Minor Paths
- Guns & when they are used
- Role of instrument and service air in Aux Boiler
- Control Systems
- Trips
Power Supplies
- Forced Draft Fan: PG11
- Fuel Oil Booster Pumps: PG19G/20B
- AS FW Pumps: PG11/12
Major/Minor Paths
- Major: Fuel; Combustion Air; Feedwater; Steam
- Minor: Blowdown; Atomizing Airstream
Guns
- Aux Gun: Up to 22% Load
- Main Gun: With Aux Gun above 22% Load
Role of Instrument and Service Air in Aux Boiler
- Service Air: provides atomizing air to Aux Gun (main uses atomizing air)
- Instrument Air: provides aspirating air to clean & seal gun not in service.
Control Systems
- Furnace Safeguards Supervisory System: provides Trips and controls for S/U & S/D.
- Combustion Control System: Controls inputs (fuel, air, feed, stm) & Outputs
Trips
- Loss of Fan
- No Pumps
- Low Drum Level (~5.25”)
- Lo atomizing pressure (75 psig)
- Hi Steam Pressure (145 psig)
- Oil Supply Pressure Low (20 psig)
- Loss of Flame (2/2 sensed)
- Both Trip Buttons
- Gun not engaged
Instrument Air Compressors
- Power Supplies to each, Rating
- Cooling to each
- How ‘C’ is different from ‘A’ & ‘B’
- Operation of KA-PV-0011
- Sequential Loading
- Compressed Air Pressure Low Alarm (92A) setpoint
- Instrument Air Dryer Pressure Low (91A) setpoint
- Unloadded Operation
- ‘A’ - NG03, ‘B’ NG04, ‘C’ - PG15; 845 scfm @ 125 psig
- ‘A’ & ‘B’ cooled by ESW; ‘C’ cooled by Chilled Water
- ‘C’ doesn’t have coolign water PCV, doesn’t have booster pump.
- KA-PV-0011 closes on 110 psig which isolates Service air.
- Compressor Loads Unloads
Lead 119 # 128 #
Lag 117 # 126 #
Standby 115 # 124 #
Positions: ABC, BCA, CAB
- 112 psig (92A)
- 105 psig (91A)
Instrument Air Dryers
- Cycle Time
- Dryer response to low pressure
- 10 minutes
- 5 minutes drying
- 5 minutes recharging
- At 105 psig on the lead dryer will cause low pressure alarm and open inlet/outlet to lag dryer & place it in service.
Reboiler Operation
- When to transfer from Aux Boiler to Reboiler & vice-versa
- Reboiler to Steam Supplies
- Feed preheating alignment
- Startup: to Reboiler between 20-30%; Shutdown: to Aux Boiler from 10-15%
- 5th Stage Extraction & Main Steam
- Extraction supplies 3-9 psig, if high load, MS supplies 9-15 psig.
- Extraction & MS isolated to reboiler, MS @ 9-15 psig si sent thru FB-HV-81 to preheat #6A/B FW Heater.
Main Feed Pump
- Nominal speed, exhaust & recircs, seal water supplies, max power on 1 MFP
- LP and HP supply and how its switched.
- How much valve position is controlled from each in “Valve Control”
- MFP Oil System Setpoints
- Turning gear controls/setpoins
- Bearing oil temp limits. Min temp to roll MFP turbine
- 5,560 RPM, A to IP B to LP exhaust, Recirc A to HP B to IP, condensate pumps (Norm) demin (Backup/Startup), 65% max power on one.
- “Low press” stem from ‘B’ MSR hot reheat line, “High press” from Main Steam cross-tie header.
- Switches to “LP” as power increases since hot reheat pressure increases. At ~40%, all steam flow is from LP.
- In valve control, first 20% attempts to use LP. To get to HP, must open past 20%.
- AP control oil (220#) to stop control valves, LP control oil (55#) to wear device, 20 # LO to pump, 12# LO to bearing. Pumps powered from (A) PG13Q/12J (B) PG12J/11K. Standby starts at 175#. Emergency at 20#. Oil Cooled by CLCW.
- Turning gear auto engages/disengages @ 2 rpm. LO @ 5 seconds. If LO Pressure < 4 psig will trip.
- Oil outlet < 180°F and ΔT < 50°F. 60°F min temp for startup.
Extraction Steam & Heater Drains (AF)
- HP Heater flow rating.
- Effect from high-high level.
- LP Heater & Extraction Steam MOVs.
- Which heaters have BTVs?
- How do other heaters prevent overspeed?
- 1st Stage Reheater DT/MSDT Interlocks?
- 2nd Stage RDT Interlocks
- Arrangement of MSR/Reheate Drain Tanks?
- Max power with LP or HP Heaters Isolated?
- 50% flow
- Extraction steam have MOVs that shut on high-high level
- Extraction steam lines to #3/#4 Htrs have MOVs that shut on Hi-Hi Level
- 3/4/6/7 have BTVs.
- Close on Hi-Hi Level
- # 5 prevented by CIVs
- # 2 has check valv
- # 1 has baffles in heater.
- Dump valve opens @ 10% power to pull air & gases to Condenser.
- Dump valve opens @ 20% power to pull air & gases to Condenser.
Extraction Steam Stages & Where they go:
Condenser Vacuum Pumps
- Power Supplies
- Connections to HVAC & What happens on SIS & Startup Alignment
- Standby Features
- Seal Water makeup and overflow
- Seal Water cooling
- Interlock
Condenser Vacuum Pumps
-
Power Supplies
- __A & C: PG11
- B: PG12
-
Connections to HVAC & What happens on SIS & Startup Alignment
- __Discharges to TB HVAC, which exhausts thru filter absorber unit on 2047’ AB. GE-RE-92 monitors exhaust for SBTR.
- On SIS dampers close -> hoggers trip. Dumpers & hoggers may be restarted on w/o resetting SI.
- On Startup, valved to exhuast to TB Atmosphere = unmonitored release & samples must be taken.
-
Standby Features
- Standby auto starts @ 5.6” HgA (23.5” HgV)
-
Seal Water makeup and overflow
- __Makeup: CST
- Overflow: Misc. Condensate Drain Tank
-
Seal Water cooling
- Service Water
-
Interlock
- __Prevents opening suction valve unless D/P < 1.5” HgA (ensures that you don’t break vacuum).
- Additionally interlocked pump w/ filter absorber discussed above.
CSDs (Condenser Steam Dumps)
- Capacity
- Where the dumps go/groups
- How to Cool Down < 550°F
- Controls
- Purpose of AC-PT-505, 506, & 507
- 528,000 lbm/hr (3.3% Steam Flow), 12 total CSDs
- 3 CSDs per Group, 4 Groups (7 CSDs to LP; 4 CSDs to IP; 1 CSD to HP)
- Group 1 & 2:
- 3 to LP
- Group 3:
- 1 to LP
- 2 to IP
- Group 4:
- 2 to IP
- 1 to HP
- Group 1 & 2:
- Pstm mode, Once Temp < P-12 (550°F), blocks CSDs, Place Stm dump bypass interlock AB-HIS-63/64 in BYP/Interlock.
- Stm Dump selector (AB-US-5002) selects:
- Tavg (Load Reject OR Plant Trip)
- Pstm
- PT-505: Make Tref for CS Control
-
PT-506: Feeds C-7 (10% stop or 5%/min for 2 min)
- Reset -> Resets C-7 (PT-506)
-
PT-507: Feeds steam pressure controller (AB-PK-507)
- 10 Turn Pot from 0-1500 psig (150psig/turn)
- 1092 psig = 7.28 turns
- 10 Turn Pot from 0-1500 psig (150psig/turn)
LP FW Heaters
- Flow rating, efficiency rise
- Extraction Point for each heater
- Max power with 1, 2, or 3 htr strings out of service
- Nominal ΔT across each heater
- Isolation Valve operation & interlocks
- Location of the heaters and arrangment
LP FW Heaters
-
Flow rating, efficiency rise
- __50% Condensate Flow
- ~15% efficiency rise
-
Extraction Point for each heater
- #1 from 16th Stage
- # 2 from 14th Stage
- # 3 from 12th Stage
- # 4 from 9th Stage
-
Max power with 1, 2, or 3 htr strings out of service
- __One: 1125 MWe
- Two: 770 MWe
- Three: 414 Mwe
-
Nominal ΔT across each heater
- __126° into #1 Heater
- 183° into #2 Heater (ΔT 57°)
- 218° into #3 Heater (ΔT 35°)
- 284° into #4 Heater (Δ 66°)
- 319° out of #4 Heater (Δ 35°)
-
Isolation Valve operation & interlocks
- __Strings have MOVs.
- Operate in pair
- High shell side level in #1 or #2 HTR will close
-
Location of the heaters and arrangment
- __Located in “Neck” of condenser
- A in LP
- B in IP
- C in HP
Hotwell Level Control & Exhaust Spray
- LT-114
- LT-79
- Hotwell makeup setpoints & process
- Condenser reject process
- Hi Hotwell Setpoint & Control
- Lo Hotwell Setpoint
- Lo-Lo Hotwell Level Setpoint & Control
- Exhaust Hood hi-temp alarm & Trip.
- Hood Spray Operation
- LT-114: __Indication on RL024
-
LT-79 Controls:
- __AD-LV-79A: to open reject @ 81” (85%)
- AD-LV-79BB: 3” Valve starts making up @ 72” (70%)
- If level continues to go down when AD-LV-79BB is full open, AD-LV-79BA (10”) opens to restore level.
-
Hi Level @ 79.5” -> Annunciator 106C
- Isolates HF-HV-62 SLW return.
- Lo level @ 55.5” -> Annunciator 106B
-
Lo-Lo level @ 49.5” -> Annunciator 106A
- 1/3 actuates alarm
- 2/3 trips all condensate pumps.
-
Exhaust Hood Spray:
- Alarm 176°F
- Trip 225°F
- Spray Full Open from 900 RPM to 10% Load
High-High Level in Heaters
- MCB Hi-Hi Level Alarm
- Close extraction steam MOVs (#1 & #2 have no MOVs)
- Bleeder Trip Valves (BTVs) close (#3/4/6/7)
- Extraction Steam Dain Valves (to condenser) Open
- Close Inputs from Reheat Drain Tanks (#6/7)
- Close Cascade drains from associated heaters
- 7 -> 6
- 4 -> 3
- 2 -> 1
- Isolates scavenging steam from MSR to #6/#7 Heaters
- Condensate isolates to LP Heater Train for Hi-Hi Level in a #1 or #2 Heater Only.
Condensate Pumps
- Power Supplies
- Bearings & Cooling
- Capacity & Power Limit
- Precautions
- Mini-flow valves & fail position
- Vents & seal water
- Pump shutoff head & feeding SG w/ Condensate Pump
-
Power Supplies
- A & C: PB03
- B: PB04
-
Bearings & Cooling
- Upper: Oil cooled by CLC
- Lower: Cooled by grease
-
Capacity & Power Limit Precautions
- Do not exceed 55 psig @ pump suction, it may rupture expansion joint.
- Maintain Polisher D/P 12-50 psid
- Condensate pumps require <155°F and 15’ Head at suction for NPSH.
-
Mini-flow valves & fail position
- Mini-flow valves start to open @ 2400 gpm.
- Linearly ramp from 0-2400 gpm.
- A to LP; B to HP; C to IP
-
Vents & seal water
- Pump suction & casing vented back to HP condenser to remove vapor.
- Startup vent on discharge returns to IP condenser
- Seals provided by pump discharge.
- Backup/startup supply from demin water.
-
Pump shutoff head & feeding SG w/ Condensate Pump
- Shutoff head 630 psig.
- To feed SG w/ Condensate pump, need SG Pressure < 553.4 psig (accounts for losses)