High-Temperature and High-Pressure Valves / China
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Cogeneration & CHP

CHP plants run at lower steam conditions than utility units but change load far more often. Cycling, not peak temperature, is the design driver.

Typical conditions

Parameter Value Basis
Live steam pressure 4-14 MPa typical typical
Live steam temperature 440-540 °C typical typical
Extraction pressure 0.3-2.5 MPa to the heat network typical
Load changes Daily and seasonal, following heat demand per project

Lower conditions, harder duty cycle

A district heating CHP plant follows heat demand, which means daily starts in the shoulder seasons and continuous load-following in winter. The steam conditions are modest - F11 or F22 usually covers the body material - but the valves see many times the cycle count of a base-load utility unit.

Extraction and back-pressure interfaces

The interface between the turbine and the heat network is where the valve work concentrates: extraction control, back-pressure isolation, and non-return protection so a network upset cannot feed back into the machine.

  • Extraction check valves sized against the turbine protection requirement
  • Isolation between the steam side and the heat network
  • Pressure-reducing station isolation, upstream and downstream

Why pressure seal still applies at moderate class

Even at Class 900, a bolted bonnet on a valve that thermally cycles daily will need gasket attention. The self-energizing bonnet removes that maintenance item. This is a stronger argument in CHP than in base-load service, where cycles are fewer.

Biomass and waste-fired variants

Biomass and waste-to-energy plants add corrosive flue-gas-side chemistry and often more aggressive steam-side conditions than the nominal parameters suggest. Where the fuel is variable, say so at enquiry - it changes the material discussion.

Materials commonly used here

  • A105N
  • A182 F11
  • A182 F22
  • WCB
  • WC6

Indicative only. The grade is set by the piping class and the ASME B16.34 rating at your design temperature - see the material matrix.

Recommended products

Pressure Seal Gate Valve

gate · pressure seal bonnet

Body
A105, A182 F11, F22, F91, F92
Size
NPS 2-24 (DN 50-600)
Class
Class 600 - 4500
Temp
up to 650 °C / 1200 °F
End
BW, SW, RTJ, RF
Standard
ASME B16.34
View specification

Pressure Seal Globe Valve

globe · pressure seal bonnet

Body
A105, A182 F11, F22, F91, F92
Size
NPS 2-16 (DN 50-400)
Class
Class 900 - 4500
Temp
up to 650 °C / 1200 °F
End
BW, SW, RTJ, RF
Standard
ASME B16.34
View specification

Stop-Check Valve

stop check · pressure seal bonnet

Body
A182 F22, F91, F92
Size
NPS 2-16 (DN 50-400)
Class
Class 900 - 2500
Temp
up to 620 °C / 1148 °F
End
BW, RTJ, RF
Standard
ASME B16.34
View specification

Frequently asked questions

Do CHP plants need creep-grade materials?

Usually not - live steam at 440-540 °C is well within F11 and F22 territory. The exception is a high-parameter industrial CHP running near 540 °C continuously, where the margin should be checked against the actual B16.34 rating rather than assumed.

What fails first in cycling service?

In our experience, bonnet gasket joints on bolted-bonnet valves, and wedges that bind after a hot shutdown. Both are addressed by construction choices - pressure seal bonnets and flexible wedges - rather than by material upgrades.

Further reading

Discuss this application

Send the system conditions and we will come back with what we would supply, the rating basis, and any point where we would question the specification.

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