1. Problem Description & Scope
Valve hunting, also called oscillation, is the phenomenon whereby a control valve continuously moves around the desired setpoint, instead of assuming a stable position. This leads to premature wear of gaskets, seats and actuators, and disrupts process stability. This guide focuses on pneumatically and digitally controlled control valves in the process industry in the Benelux. Severity ranges from small fluctuations affecting process quality (minor) to complete instability leading to process shutdown (critical).
2.Safety Precautions
WARNING: Control valves are under process pressure and often under high pneumatic pressure. Before beginning any diagnostics or maintenance: Perform strict Lockout/Tagout (LOTO) procedures. Relieve all stored energy, both process pressure and instrument air. Always use the prescribed Personal Protective Equipment (PPE), including eye protection, hearing protection and gloves suitable for the process media. Be alert to hot surfaces and potentially toxic process gases or liquids.
3.Diagnostic Tools Required
| Tool | Specification | Measuring range | Goal |
|---|---|---|---|
| Multimeter | True RMS, industrial quality | mA, V, Ohm | Check 4-20mA signal and power supply |
| Manometer (Accurate) | Calibration class 0.5% | 0-10 bar | Measuring instrument air and actuator pressure |
| Vibration analyzer | Handheld, FFT analysis | 0-50mm/s | Detecting mechanical oscillation |
| Infrared Thermometer | Class II | -20 to 500 °C | Detecting friction due to heat |
| Communicator (HART) | Industrial standard | N/A | Diagnosis of digital positioner settings |
4. Initial Assessment Checklist
| Check | Goal |
|---|---|
| Is the oscillation visible in the SCADA system? | Determine if the problem is electrical or mechanical |
| Does the oscillation change when the setpoint changes? | Distinguish between stiction and process instability |
| What is the pressure of the instrument air? | Check for stable power supply |
| Are there any recent changes to the PID tuning? | Excluding software causes |
5. Systematic Diagnosis Flowchart
- Analyze the signal (PV vs. CO):
- If the valve position (CO) is stable, but the process (PV) is oscillating: Process instability (PID tuning in the controller).
- If the valve position (CO) oscillates: Go to step 2.
- Check for mechanical friction (Stiction):
- Increase the signal in small steps (0.5%). If the valve suddenly jumps: Too high friction (gasket).
- Check instrument air and actuator:
- Pressure drop in instrument air? Leakage or filter blockage.
- Leakage in actuator membrane? Actuator damage.
- Check positioner settings:
- Gain too high? Decrease gain.
- Dead zone too small? Enlarge dead zone.
6. Fault-Cause Matrix
| Symptom | Probable Cause | Diagnostic Test | Expected Result |
|---|---|---|---|
| Sudden jumps | Stiction (gasket) | Manual step increase | Jerky movement |
| Fast, constant oscillation | Positioner gain too high | HART diagnostic gain setting | Gain is above recommended value |
| Slow oscillation | PID tuning process controller | Analysis PV vs CO graph | PV is ahead of CO |
| Valve does not reach set point | Actuator leakage | Pressure gauge on actuator | Pressure drops at constant load |
7. Root Cause Analysis
7.1 Stiction (Static Friction)
Stiction occurs when the friction force between the valve stem and the packing exceeds the force the actuator can provide for small changes. This results in the infamous stick-slip effect. Causes: over-tightened gasket, corrosion on the stem, or wrong type of gasket for the application. This leads to rapid wear of both the valve stem and the actuator.
7.2 Positioner Tuning
Digital positioners use algorithms to control the valve position. Too high a gain (amplification) responds too aggressively to small deviations, leading to overcorrection and oscillation. Too small a dead zone (deadband) causes the positioner to try to correct for noise in the signal, which causes unnecessary wear.
7.3 Process Interaction
If the time constant of the process (e.g. liquid level in a large tank) is faster than the valve response time, a feedback loop instability occurs. The valve chases the process.
8. Step-by-Step Resolution Procedures
8.1 Gasket adjustment
- Lock/Mark: Make the valve safe in accordance with LOTO.
- Pressure relief: Ensure that there is no longer any process pressure on the valve.
- Adjustment: Carefully loosen the packing nut. Check that the movement is smooth. Re-tighten to point of seal, no tighter than necessary (use torque wrench if specified by OEM).
- Verification: Perform an air leak test at maximum process pressure.
8.2 Positioner Tuning
- Use a HART communicator to read the current parameters.
- Decrease the 'Proportional Gain' in 10% increments until the oscillation stops.
- Increase the 'Deadband' step by step (e.g. from 0.1% to 0.5%) to see if the oscillation decreases without losing too much accuracy.
- Perform an 'Auto-tuning' cycle if the positioner supports it, but always check the results manually.
9. Preventive Measures
| Root Cause | Prevention Strategy | Monitoring Method | Interval |
|---|---|---|---|
| Stiction | Regular lubrication/maintenance | Visual inspection stem | 6 months |
| Positioner | Create backup settings | HART check for abnormalities | 12 months |
| Actuator air | Filter/Dry | Check condensation in air filter | 3 months |
10. Spare Parts & Components
| Part Description | Specification | When to replace | UNITEC Category |
|---|---|---|---|
| Gasket set (PTFE/Graphite) | Specific to valve model | With every overhaul/leakage | Valve seal |
| Digital Positioner | HART 7, ATEX certified | In case of electronic failure | Instrumentation |
| Membrane Actuator | EPDM or Viton | Every 3-5 years | Actuator parts |
For all necessary spare parts, visit: https://www.unitecd.com/e-catalog/
11.References
- NEN-EN 13445: Pressure equipment.
- ISO 9001: Quality management systems (process control).
- OEM manuals from the specific valve manufacturer.