Balance of Plant (BOP)¶
The balance-of-plant systems convert main-steam energy to electrical output and return feedwater to the steam generators. From an EOP perspective the BOP is relevant as the normal heat sink (turbine + condenser + main feedwater) whose loss drives the plant onto AFW and on to the secondary-side heat-removal recovery procedures (E-0, FR-H.1).
Function¶
In normal operation: main-steam from the four SGs drives the HP and LP turbines; exhaust steam condenses in the condenser against circulating water; condensate is pumped through low-pressure heaters, the deaerator, and the main feedwater pumps back to the SGs at ~440 °F through high-pressure heaters.
In transient response: a turbine trip closes the turbine stop valves and dumps steam to the condenser via the dump valves (if condenser available); main feedwater isolates on SI; AFW takes over SG feed. Loss of condenser vacuum forces atmospheric dumping via ARVs.
Components¶
flowchart LR
MS["Main Steam<br/>(from 4 SGs)"]
TSV["Turbine Stop Valves<br/>«TSV-POS»"]
HP_T["HP Turbine"]
MSR["Moisture Separator<br/>Reheaters"]
LP_T["LP Turbines<br/>(3 stages)"]
GEN[("Main Generator<br/>«GEN-MW»")]
COND["Condenser<br/>«COND-VAC»<br/>«COND-LVL»"]
DUMP["Condenser Dump Valves<br/>«COND-DUMP-VLV»"]
CW["Circulating Water<br/>(cooling tower or<br/>once-through)"]
HOTWELL["Hotwell"]
CP_A(("«COND-PUMP-A»"))
CP_B(("«COND-PUMP-B»"))
LP_HTR["LP Feedwater Heaters<br/>(4 stages)"]
DEAER["Deaerator"]
MFP_A(("«MFP-A»"))
MFP_B(("«MFP-B»"))
HP_HTR["HP Feedwater Heaters<br/>(2 stages, ~440 °F)"]
FWI["MFW Isolation<br/>«MFW-ISOL»"]
SG["To SGs"]
MS --> TSV --> HP_T --> MSR --> LP_T --> GEN
LP_T --> COND
MS -. "turbine bypass" .-> DUMP --> COND
COND --> HOTWELL
CW -. cooling .-> COND
HOTWELL --> CP_A & CP_B --> LP_HTR --> DEAER --> MFP_A & MFP_B
MFP_A & MFP_B --> HP_HTR --> FWI --> SG
classDef turbine stroke:#856404,stroke-width:2px
classDef pump stroke:#1f618d,stroke-width:2px
classDef vessel stroke:#6c3483,stroke-width:2px
class HP_T,LP_T,GEN turbine
class CP_A,CP_B,MFP_A,MFP_B pump
class COND,HOTWELL,DEAER vessel
- Main turbine — tandem-compound HP + 3 LP stages; ~1180 MWe gross at Vogtle; moisture-separator-reheaters between HP and LP for saturated-steam cycle.
- Main generator — direct-coupled to turbine shaft; hydrogen-cooled stator; output to switchyard via main transformer.
- Condenser — multi-shell surface condenser; saturated steam condenses at ~3 in Hg abs (about 100 °F); circulating water cools the shell side.
- Condenser steam dump valves — bypass steam from main steam header directly to condenser; capacity sized for 100% load rejection at Vogtle (≈40% steam-flow dump).
- Condensate pumps — typically two, vertical multistage; pump hotwell condensate up through the LP feedwater heaters.
- Deaerator — strips dissolved oxygen from condensate; provides NPSH for main feedwater pumps; storage volume for transient flow mismatch.
- Main feedwater pumps — typically turbine-driven, two pumps; full flow on both; ~16000 gpm each at full load.
- HP feedwater heaters — final feed temperature ~440 °F; isolated on FWI signal (string check valves) to prevent heater-source inventory from flooding the SG.
- Main feedwater isolation valves — close on SI / FWI; AFW takes over SG feed via separate nozzles.
Instrumentation¶
- Generator output: «GEN-MW»
- Turbine stop valve position: «TSV-POS»
- Condenser vacuum: «COND-VAC»
- Hotwell level: «COND-LVL»
- Condenser dump valve position: «COND-DUMP-VLV»
- Condensate pump statuses: «COND-PUMP-A», «COND-PUMP-B»
- MFW pump statuses: «MFP-A», «MFP-B»
- MFW isolation valve position: «MFW-ISOL»
- MFW flow per SG: «MFW-FLOW-SG-A»…D
Setpoints¶
| Parameter | Value | Source |
|---|---|---|
| Rated thermal power | 3625 MWt | Vogtle UFSAR §1.3 |
| Gross electrical output | ~1180 MWe | Vogtle UFSAR §1.3 |
| Condenser design vacuum | ~3 in Hg abs (100 °F) | Vogtle UFSAR §10.4.1 |
| Condenser steam dump capacity | ~40% MS flow | Vogtle UFSAR §10.4.4 |
| MFW final feed temperature | ~440 °F | Vogtle UFSAR §10.4.7 |
| MFW isolation on SI | automatic | Vogtle UFSAR §10.4.7 |
| Loss-of-condenser-vacuum trip | «COND-VAC» < 22 in Hg | Vogtle Tech Spec 3.3.1 |
Normal alignment¶
- Turbine on line at rated load; generator synced to grid
- Both condensate pumps and both MFW pumps in service
- Condenser dump valves closed; available on demand
- Deaerator at LCO storage level
- MFW isolation valves open; AFW pumps standby
Failure modes¶
- Loss of condenser vacuum — sealing water failure, air in- leakage, CW loss. Turbine trips at «COND-VAC» < setpoint; steam dump unavailable; ARVs become the only steam-relief path. Cross- links to FR-H.1 (heat sink threats).
- MFW pump trip / both — feed flow lost; AFW automatic actuation on low-low SG level. Response embedded in E-0 / ES-0.1.
- Loss of circulating water — cooling tower or intake failure; condenser pressure climbs; turbine trip via vacuum interlock.
- Generator load rejection — sudden grid disconnect; turbine overspeed protection trips; steam dump must handle full load rejection or SG safeties lift.
- Feedwater heater string isolation — HP heaters trip; feed temp drops, increasing reactor power demand; runback or trip may follow.
Relationship to EOPs¶
BOP loss is the dominant initiator of secondary-side EOP entry: turbine trip + MFW loss drives the plant to AFW heat removal. Most recovery flows (FR-H.1 / FR-H.2 / FR-H.4) treat BOP restoration as a long-term recovery path; the immediate EOP focus is on AFW and steam-relief integrity rather than restoring the turbine cycle.
References¶
- Vogtle UFSAR §10.1 (Summary description — steam and power conversion)
- Vogtle UFSAR §10.2 (Turbine generator)
- Vogtle UFSAR §10.4.1 (Main condenser)
- Vogtle UFSAR §10.4.4 (Turbine bypass steam dump)
- Vogtle UFSAR §10.4.7 (Condensate and feedwater)
- Vogtle Tech Spec 3.3.1 (Reactor protection trip — vacuum)