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Boiler Drain & Blowdown Expansion System (Flash Tanks): Principles and Design Essentials

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.


Quick engineering comparison

DimensionDFT (Startup Drains)IBFT (Intermittent Blowdown)CBFT (Continuous Blowdown)
SourceECO/SH/RH/MSL drains during start/low loadDrum/bottom blowdown pulsesDrum surface blowdown, steady
Flow characterEpisodic, high vapor fractionHigh instantaneous flow, solids-bearingSmall, continuous, PLC/DCS modulated
Design emphasisSafe venting & separationErosion resistance, quench-cooled dischargeHeat recovery, stable control with DA/BDHR
Steam destinationAtmosphere silencer or DA/LP headerAtmosphere/DA (with silencer)Prefer DA/LP header
ControlsLIC→LV (level), PT, PSVLIC→LV, TIC→quench CV, PT, PSVAIT(Cond)→AIC→CV-BD (primary), LIC→LV, PT, PSV

Abbrev.: DA=Deaerator; BDHR=Blowdown Heat-Recovery Exchanger; LIC/LV=Level controller/valve; AIT/AIC=Conductivity indicator/controller; PT/PSV=Pressure transmitter/safety valve.


Operating principle & sizing cues

Flashing & separation

Hot pressurized water enters a vessel at lower pressure PtankP_{tank}, producing flash steam. Approximate flash quality:

xh1hf(Ptank)hfg(Ptank)x approx frac{h_1 - h_f(P_{tank})}{h_{fg}(P_{tank})}

where h1h_1 is inlet specific enthalpy, hfh_f saturated liquid enthalpy at PtankP_{tank}, and hfgh_{fg} latent heat at PtankP_{tank}.
Use xx to size steam outlet, silencer, and DA capacity; the liquid leg sizes the bottom outlet/heat-recovery path.

Vessel pressure & volume

  • 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.

Noise & temperature compliance

  • 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.


P&ID essentials

DFT (Startup drains)

  • 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.

IBFT (Intermittent blowdown)

  • 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.

CBFT (Continuous blowdown)

  • Upstream control: Boiler water conductivity loopAIT(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.


Materials & fabrication

  • 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.