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Drain Flash Tank (DFT) — handles boiler startup/low-load drains from economizer, superheater, reheater, and main steam lines; provides pressure let-down and steam–water separation, with optional heat recovery.
Intermittent Blowdown Flash Tank (IBFT) — receives pulsed bottom blowdown from the drum/headers; focuses on flash separation and safe cooling to meet site discharge limits.
Continuous Blowdown Flash Tank (CBFT) — receives steady, small-flow surface blowdown; emphasizes stable heat recovery (flash steam → deaerator/LP header; concentrated brine → blowdown heat-recovery exchanger).
Common synonyms: Expansion tank/vessel; Blowdown tank; CBD/IBD flash tank.
Abbrev.: DA=Deaerator; BDHR=Blowdown Heat-Recovery Exchanger; LIC/LV=Level controller/valve; AIT/AIC=Conductivity indicator/controller; PT/PSV=Pressure transmitter/safety valve.
Hot pressurized water enters a vessel at lower pressure , producing flash steam. Approximate flash quality:
where is inlet specific enthalpy, saturated liquid enthalpy at , and latent heat at .
Use to size steam outlet, silencer, and DA capacity; the liquid leg sizes the bottom outlet/heat-recovery path.
Tank pressure:
DFT/IBFT: balance safe venting with any heat-recovery target.
CBFT: match DA pressure (e.g., ~0.10–0.30 MPa(g)) to maximize recovery.
Effective volume: cover peak incoming pulse (IBFT) or short-term surge (DFT/CBFT) plus margin to secure separation residence time.
Top vent to atmosphere → vent silencer and velocity check.
Bottom effluent temperature per site code (often ≤60 °C): IBFT/CBFT typically include TIC→cooling water control valve.
Inlet manifold: ECO/SH/RH/MSL branches with isolation + check valves; internal distributor/deflector to reduce carry-over.
Instruments: LG/LT→LIC→LV for level; PT for pressure; PSV on top head.
Connections: Flash steam → DA/LP header or silenced vent; bottoms → condensate recovery; maintenance blowdown/drain (BDV) provided.
Inlet: From drum bottom blowdown valve; recommend tangential entry/spray distributor and wear-resistant liners.
Cooling: TIC→quench water CV to meet discharge temperature.
Others: Same safety/instrument scheme as DFT, with greater focus on erosion and thermal-shock mitigation.
Upstream control: Boiler water conductivity loop — AIT(Cond)→AIC→CV-BD modulates CBD rate.
Heat-recovery chain: Flash steam → DA; bottoms → BDHR → cooler → compliant discharge or reuse.
Level loop: LIC→LV to avoid entrainment and steam short-circuiting.
Shell & heads: SA-516 Gr.70 (or equivalent high-quality carbon steel).
Nozzle necks: SA-106 Gr.B; Flanges: SA-105.
Internals / wear parts: 304 or 410 SS as service requires; optional cladding/overlay (e.g., Alloy 625) at high-erosion zones.
Good wording for specs:
“Vessel fabricated from SA-516 Gr.70; nozzle necks SA-106 Gr.B; flanges SA-105; internals 304 SS.”
Additional good practice: corrosion allowance sized for service, qualified weld procedures (GTAW/SMAW common), NDE per code (e.g., RT/UT for butt joints, PT/MT for fillets), and proper supports/nozzle load checks for site piping.
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