Published December 16, 2013

Critical Control Valve Considerations for the LNG Market

The relatively recent rise in demand for liquefied natural gas, or LNG, has fueled a boom with regards to the construction of import and export terminals.

By Loyd Hilliard


Current LNG Processes

  1. inlet feed gas control valve
  2. rich amine letdown control valve
  3. amine pump recycle control valve
  4. gas to flare control valve
  5. compressor anti-surge control valve and
  6. Joule-Thomson/expander bypass control valve

Inlet Feed Gas Control Valve

Rich Amine Letdown Control Valve

Amine Pump Recycle Control Valve

  1. Facilitate start-up and commissioning of acid absorber unit
  2. Boost suction pressure of pump to ensure that it is above amine vapor pressure
  3. Protect pump from cavitation damage

Gas to Flare Control Valve

With service conditions characterized by high pressure drops and flow rates, this valve’s primary purpose is to safeguard the process against overpressure.

Compressor Anti-Surge Valve

The best valve body solution is a large angle construction outfitted with slotted or drilled-hole noise attenuation trim. Although it is common to impose an 85 dB(A) sound pressure level limit, this requirement is not critical as the valve operation is extremely intermittent – or at least it should be.

The criticality of this valve necessitates conducting a factory acceptance test (FAT) to verify the performance characteristics of the fully assembled valve unit. Because of the inherent complexity of the instrumentation package, it is also advisable to have some type of field acceptance test to confirm that the integrity of the unit was maintained during shipping.

Joule-Thomson / Expander Bypass Valve

Summary

Early understanding of technical challenges and proven solutions improves the mitigation of project schedule risk and potential construction or commissioning delays. Providing effective and reliable protection of critical and costly equipment is of the utmost importance. Control valve failure or sub-optimal performance can shut down a complete LNG train, and with gross revenues ranging from $16 million to $20 million per day, that simply isn’t an option.

Loyd Hilliard is severe service business manager at Puffer-Sweiven. Contact him at Loyd.Hilliard@puffer.com.

All images courtesy of Emerson Process Management

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