Industrial Control Valve

Control Valves in Power Generation: Feedwater, Bypass, Attemperator and Condensate Duty

Published · Updated · KOSA Valve Application Engineering

Power plant valves work at the edge of the envelope: high pressure, high temperature, high ΔP, and a duty cycle that goes from full flow to minimum overnight. Each service in the water-steam cycle has a distinct set of requirements.

Service-by-service requirements

ServiceTypical conditionsKey requirementsTypical selection
Boiler feedwater control150–300 bar, 200–280 °C, high ΔP at low loadWide rangeability, Class V shut-off, anti-cavitation trim, hardened plugGlobe, cage-guided, multi-stage trim, WC9 or 316 body
Feed pump minimum-flow recirculationFull pump ΔP (200+ bar) to a low-pressure deaeratorExtreme ΔP in one valve, severe cavitationMulti-stage labyrinth or stacked-disc trim; often an angle body
HP turbine bypassMain steam 180 bar / 540 °C to condenser pressureClass V shut-off, very fast stroke, low noise, thermal shock resistanceAngle or globe with multi-stage low-noise trim and steam conditioning
Superheater / reheater attemperatorWater at feed pressure into steam lineFine control at low flow, tight shut-off to avoid quenchingGlobe with low-Cv trim, Class V, variable-orifice or spring-loaded nozzle design
Condensate and heater drainLow ΔP, large volume, two-phaseFlashing tolerance, erosion-resistant trimGlobe or eccentric rotary plug, hardened trim
Deaerator level and pressureLow pressure steamStable modulation, low noiseGlobe or butterfly, Class IV

Feedwater: the rangeability problem

A drum boiler may need 3:1 to 5:1 turndown on feedwater, and a once-through or sliding-pressure unit considerably more. At low load the pump is still generating near-full pressure while the required flow is small, so the feedwater valve sees its maximum ΔP at its minimum Cv — exactly where cavitation and trim wear are worst. The standard answer is a multi-stage cage trim that splits the drop so no stage reaches vapour pressure, combined with a rangeability check at the minimum flow point rather than only at the design point.

Check: calculate the cavitation index at minimum flow with maximum ΔP, not at the design point. Most feedwater trim failures occur in a duty condition that was never modelled.

Turbine bypass: the hardest valve in the plant

A turbine bypass valve must (a) pass full main-steam flow to the condenser, (b) hold Class V shut-off against full main-steam pressure when closed, (c) stroke in 2–5 seconds on a trip, (d) survive a thermal shock from ambient to 540 °C, and (e) do all of it within the site noise limit. The design that satisfies all five is an angle or globe body with a multi-stage pressure-reducing trim followed by a diffuser, sometimes combined with downstream water injection for steam conditioning. Seat leakage is not cosmetic here — a leaking bypass bleeds expensive water and erodes the seat within weeks.

Material and construction notes

Commissioning and condition monitoring

  1. Capture a baseline step response and stroke time at hot and cold conditions — hot stroke times differ materially from cold.
  2. Install a permanent acoustic or vibration monitor on the bypass and feedwater valves; it detects cavitation onset long before the trim is damaged.
  3. Track the recorded valve position against the heat balance — a valve that has drifted to a higher opening for the same load has either a worn trim or a fouled strainer.

Our power industry solutions cover feedwater, bypass and attemperator valves with full sizing and documentation packages.

Frequently Asked Questions

Why is the boiler feedwater control valve so prone to cavitation?

At low boiler load the feed pump still delivers close to full pressure while the required flow is small, so the valve must absorb a very large pressure drop at a small opening. That combination produces the lowest cavitation index in the whole cycle. Multi-stage anti-cavitation trim is the standard mitigation.

What leakage class is required for a turbine bypass valve?

Class V to ANSI/FCI 70-2 is the usual requirement because the valve holds full main-steam pressure when closed. Any leakage continuously wastes treated water and erodes the seat, quickly turning a small leak into a large one.

Why use an angle valve for feedwater recirculation?

An angle body gives a natural, smoother flow path with a larger outlet volume, which lowers the outlet velocity and reduces the erosive effect of flashing. It also drains better and is mechanically well suited to the very high pressure drop of a pump minimum-flow duty.

How can I detect cavitation before it damages the valve?

Acoustic emission or high-frequency vibration monitoring on the valve body detects the broadband signature of bubble collapse well before measurable metal loss occurs. It is also useful to trend the relationship between valve opening and load, and to calculate the pressure profile at off-design conditions during the specification stage.

Need a valve sized for your duty?

Send us the process data — fluid, inlet pressure, differential pressure, temperature, required flow and pipe size — and our engineers will return a sized selection with Cv calculation, leakage class and material recommendation, plus documentation packs for FAT / IQ-OQ.

Request a valve sizing quote

feedwater control valveturbine bypassattemperator valvepower plant valveboiler feed pump recirculationClass V

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