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Control Valve Fail Position Failures in Chemical Plants

Table of Contents

— From the Perspective of THINKTANK Control Valve Engineers

Why we do not define control valve reliability by normal operation

As engineers at THINKTANK, we are often involved after a plant trip has already occurred.

In many of these cases, the control valve is reported as “working normally” before the incident:

  • The valve responded correctly to the controller
  • The stroke feedback matched the DCS output
  • No abnormal noise or sticking was observed

Yet the plant still tripped.

From our experience, this usually means one thing:

The valve was never verified for abnormal conditions — only for normal control.

A control valve does not prove its safety during stable operation.
It proves its safety at the moment when signal, power, or air is lost.

control valve failure modes
control valve failure modes

How we explain the real meaning of “fail position” to customers

When we review control valve specifications with customers, we always clarify one point early:

A fail position is not a mechanical guarantee.
It is an engineering assumption that must be validated on site.

In chemical plants, typical fail actions include:

  • Fail Open (FO)
  • Fail Close (FC)
  • Fail Lock Open (FLO)
  • Fail Lock Close (FLC)

These definitions describe what the valve should do when a failure occurs.
They do not describe what the valve will actually do unless the entire control chain behaves as expected.

This control chain includes:

  • DCS analog output behavior
  • Positioner power and configuration logic
  • Pneumatic routing
  • Actuator fail direction

If any part of this chain behaves differently, the fail position shown on drawings becomes meaningless.

control valve fail mode image
control valve fail mode image

A signal-loss accident we frequently help customers analyze

One typical case we have seen in chemical plants occurs during normal operation, not during startup.

What happened on site:

  • The DCS output dropped below the minimum signal range required by the smart positioner
  • The positioner lost power
  • According to design, the valve should have failed closed
  • In reality, the valve remained fully open
  • The unit tripped immediately

What the plant team initially believed:

“Signal loss should automatically lead to fail action.”

What we found during engineering analysis:

  1. During commissioning, only loop checks and stroke calibration were performed
  2. Signal-loss behavior was never physically tested
  3. The positioner’s direct/reverse action had been modified to correct indication mismatch
  4. The impact of this change on fail behavior was never revalidated

The valve functioned perfectly — until it was required to fail safely.

Why loop checks and stroke tests do not reveal this risk

Many commissioning procedures focus on:

  • Agreement between DCS output and valve position
  • Linear response over the full stroke
  • Stable behavior in auto mode

These tests confirm control accuracy, not failure behavior.

A signal-loss accident cannot be detected unless the test deliberately creates:

  • Complete signal interruption
  • Positioner power loss
  • Independent air failure

If these conditions are not tested, fail behavior exists only as a theoretical assumption.

calibration of control valve (3)

Smart positioners: accuracy improvement with hidden failure paths

Smart positioners significantly improve control performance, but they also introduce configuration risks.

In the field, we often see adjustments made to:

  • Direct / reverse action
  • Input signal range
  • Internal logic parameters

These changes are usually made to solve indication or tuning issues.
However, they can silently alter how the valve behaves when power or signal is lost.

This explains why many fail-position accidents occur months after commissioning, not during initial startup.

How THINKTANK engineers troubleshoot signal-loss failures

When we support customers facing this issue, we do not immediately replace equipment.

We start by verifying failure logic, step by step.

First, we test true signal loss

  • Forcing the AO below the positioner operating range
  • Observing actual valve movement, not expected behavior

Second, we separate failure modes

  • Signal loss
  • Power loss
  • Air loss

Each condition is tested independently.

Third, we review the complete control chain

  • DCS AO action logic
  • Positioner configuration
  • Actuator fail direction
  • Pneumatic connections

Only after this analysis do we decide whether hardware changes are required.

control valve after service team1

Engineering corrections we typically recommend

When THINKTANK engineers are involved in troubleshooting signal-loss accidents, our corrections focus on making failure behavior predictable, not simply restoring normal control.

Based on repeated field experience in chemical plants, we typically recommend the following engineering corrections.

First, fail-position behavior must be physically verified, not assumed.
Each control valve should be tested under true abnormal conditions, including:

  • complete loss of control signal,
  • loss of positioner power,
  • and loss of instrument air.

Fail action should be confirmed by observing real valve movement on site, not inferred from configuration settings or drawings.

Second, the action logic across the control chain should be kept as simple and consistent as possible.
From our experience, unnecessary action reversals are a common source of signal-loss failures.

We generally recommend:

  • configuring the DCS analog output (AO) as direct acting for air-to-open valves,
  • configuring the DCS AO as reverse acting for air-to-close valves,
  • keeping the field-mounted valve positioner in direct acting mode whenever possible,
  • and performing any required logic inversion at higher system levels rather than inside the positioner.

This approach makes fail behavior easier to understand, easier to test, and less sensitive to configuration changes.

Third, any change to positioner configuration must trigger a mandatory fail-position retest.
Adjustments such as:

  • direct/reverse action changes,
  • signal range modification,
  • or internal logic tuning

may not affect normal control, but they can fundamentally change valve behavior during signal or power loss.
These changes should never be accepted without re-verifying fail action.

Fourth, DCS output limits should be engineered deliberately.
Minimum AO values should be defined to avoid unintended positioner power loss, unless loss of signal is intentionally used as part of the safety logic.
Uncontrolled AO drop is a common and often overlooked cause of fail-position accidents.

Finally, fail-behavior verification should be treated as an acceptance requirement, not a commissioning formality.
We recommend documenting fail-position test results as part of the valve handover package, especially after maintenance, re-piping, or accessory replacement.

From our perspective, these corrections are not complex.
They simply enforce a basic engineering principle:

A control valve is only reliable when its failure behavior is fully understood, tested, and repeatable.

Our engineering conclusion

From the THINKTANK engineering perspective, control valve accidents rarely result from poor valve design.

They result from unverified assumptions hidden inside systems that appear to work perfectly.

A control valve is safe not because it controls well,
but because it fails exactly as engineers expect.

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Picture of Will Don

Will Don

After earning my bachelor's degree in mechanical engineering from Zhejiang Normal University in 2008, l was fortunate enough to begin my career with Siemens, Fisher, and YTC, focusing on control valve accessories. Over the past dozen years, l've poured my heart and energy into understanding technology and fluid solutions for control valves.
Now, as the marketing director for THINKTANK, a trusted branch of the Taiwan STONE valve group, I can't help but feel proud of how far we've come.
Our knowledge isn't just reaching professionals like engineer and valve distributors; it's also inspiring the next generation of automation college students.
l genuinely hope you're enjoying our articles and finding them helpful. Your thoughts, questions, and feedback mean the world to me, so please don't hesitate to reach out to [email protected]. Whether you're a seasoned expert or just curious about the field, I'm here to connect, share, and learn together.

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I am the author of this article, and also the CEO and marketing director of THINKTANK, with 15 years of experience in the industrial valve industry. If you have any questions, you can contact me at any time.

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