Self-Operated Pressure Control Valve Failure Mode: Understanding Fail Open (FO) and Fail Close (FC) - Just Measure it

Self-Operated Pressure Control Valve Failure Mode: Understanding Fail Open (FO) and Fail Close (FC)

Introduction

When selecting a control valve, engineers often need to consider its failure position, such as Fail Open (FO) or Fail Close (FC).

For conventional pneumatic control valves, the failure position can usually be selected by changing the actuator action, spring arrangement, or valve configuration.

However, the situation is different for self-operated pressure control valves (self-regulating valves).

The failure position of a self-operated pressure control valve is normally determined by its working principle, valve structure, and application type. It is not freely selectable like a pneumatic control valve.

In general:

  • Pressure reducing self-operated valves → Fail Open (FO)
  • Back pressure self-operated valves → Fail Close (FC)

The failure mode is an inherent characteristic of the valve design.

1. Failure Position Cannot Be Freely Selected

Unlike pneumatic control valves, self-operated pressure control valves do not use an external energy source such as compressed air.

The driving force comes directly from the process medium pressure, while the spring provides the restoring force.

When the sensing pressure or driving force is lost due to conditions such as:

  • diaphragm failure
  • impulse line damage
  • loss of process pressure

the spring force moves the valve plug to its natural safe position.

Therefore, the final failure position is determined by the valve design.

ItemPneumatic Control ValveSelf-Operated Pressure Control Valve
Energy sourceExternal air supplyProcess medium pressure
FO / FC selectionUsually selectableDetermined by valve type
Adjustment methodActuator action and valve configurationValve structure
Failure positionDesigned according to process safety requirementsNatural characteristic of the valve

2. Self-Operated Valve vs Pneumatic Control Valve

A pneumatic control valve normally requires:

  • actuator
  • positioner
  • instrument air supply
  • control signal

The failure mode can be configured as:

  • Air-to-open → Fail Close
  • Air-to-close → Fail Open

For a self-operated pressure control valve, no external control signal or air supply is required.

The valve automatically responds to pressure changes through:

  • sensing diaphragm
  • spring force
  • internal valve plug movement

Therefore, its failure position cannot simply be changed by selecting actuator action.

3. Failure Position of Different Types of Self-Operated Pressure Control Valves

3.1 Pressure Reducing Self-Operated Valve (Downstream Pressure Control)

A pressure reducing valve is used to maintain a stable downstream pressure.

Typical applications:

  • steam pressure reduction
  • nitrogen supply systems
  • utility gas pressure control
  • cooling water pressure control

Working Principle

During normal operation:

 
Downstream pressure increases
          ↓
Diaphragm sensing force increases
          ↓
Spring is compressed
          ↓
Valve closes slightly
          ↓
Downstream pressure remains stable
 

When the sensing pressure is lost:

 
Driving force disappears
          ↓
Spring returns to original position
          ↓
Valve opens
          ↓
Fail Open (FO)
 

Therefore:

Pressure reducing self-operated valve = Fail Open (FO)

3.2 Back Pressure Self-Operated Valve (Upstream Pressure Control)

A back pressure valve is used to maintain a stable upstream pressure.

Typical applications:

  • tank pressure control
  • pressure relief applications
  • upstream pressure stabilization

Working Principle

During normal operation:

 
Upstream pressure increases
          ↓
Diaphragm force increases
          ↓
Valve opens
          ↓
Upstream pressure is released
 

When the sensing pressure is lost:

 
Driving force disappears
          ↓
Spring returns
          ↓
Valve closes
          ↓
Fail Close (FC)
 

Therefore:

Back pressure self-operated valve = Fail Close (FC)

4. Explanation from Engineering Standards

According to SH/T 3180-2016, the failure modes of control valves and self-operated control valves should follow:

  • Back pressure control → Fail Close
  • Pressure reducing control → Fail Open

API Standard 614 also states:

Unless otherwise specified on the schematics, failure mode for control valves are:

  • Backpressure: Fail Closed
  • Pressure reducing: Fail Open

These requirements are consistent with the natural characteristics of self-operated pressure control valves.

5. Classification of Self-Operated Pressure Control Valves

ItemPressure Reducing ValveBack Pressure Valve
Control targetDownstream pressureUpstream pressure
English namePressure Reducing RegulatorBack Pressure Regulator
FunctionReduce and stabilize downstream pressureMaintain upstream pressure
Valve actionNormally pressure-close typeNormally pressure-open type
Failure positionFail Open (FO)Fail Close (FC)
Pressure sensing pointDownstream sideUpstream side
Typical applicationGas supply, nitrogen blanketingTank pressure control, pressure release

6. Important Considerations in Engineering Applications

Because the failure position of a self-operated pressure control valve cannot be freely selected, engineers must select the correct valve type according to process safety requirements.

The selection principle is:

Safety RequirementRecommended Valve TypeFailure Position
Continuous flow required during failurePressure reducing valveFO
Media isolation required during failureBack pressure valveFC
Neither FO nor FC meets the requirementUse pneumatic control valveAdjustable

If the required safety action conflicts with the natural failure position of a self-operated valve, a self-operated valve should not be selected.

7. Application Example: Nitrogen Blanketing System

In nitrogen blanketing systems, both pressure reducing valves and back pressure valves are commonly used.

The pressure reducing valve supplies nitrogen into the tank, while the back pressure valve controls tank pressure and releases excess gas.

A common design consideration:

If the set points of the pressure reducing valve and back pressure valve are too close, nitrogen supply and exhaust functions may counteract each other.

Therefore, the back pressure valve set point should normally be higher than the pressure reducing valve set point to avoid unstable operation.

Conclusion

Self-operated pressure control valves do not have a freely selectable FO or FC failure mode like pneumatic control valves.

Their failure position is determined by:

  • valve function
  • sensing pressure location
  • internal mechanical design

In general:

  • Pressure reducing self-operated valve → Fail Open (FO)
  • Back pressure self-operated valve → Fail Close (FC)

During engineering design, the correct valve type should be selected according to process safety requirements. If the required failure action does not match the natural characteristic of a self-operated valve, a pneumatic control valve with a configurable failure position should be considered.

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