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Cryogenic Valve Design and LNG Applications

Cryogenic valves must maintain leak-tight performance from ambient temperature down to -196 degrees C for liquid nitrogen, LNG and LPG service. This guide covers extended-stem design, low-temperature material qualification, standards and testing requirements.

cryogenic valveLNG valveliquid nitrogenextended stemBS 6364low temperature valveASME B16.34

In This Article

  1. 1.What Makes a Valve Cryogenic?
  2. 2.Extended-Stem (Cold-Box) Design
  3. 3.Low-Temperature Material Qualification
  4. 4.Seat and Seal Materials
  5. 5.Cryogenic Testing Requirements
  6. 6.Valve Types for LNG Service
  7. 7.LNG Project Valve Specifications

What Makes a Valve Cryogenic?

A cryogenic valve is specifically designed, tested, and certified for reliable operation at temperatures below -46 degrees C, with the most demanding applications reaching -196 degrees C for liquid nitrogen and liquid oxygen and -162 degrees C for LNG at atmospheric pressure. Standard industrial valves are not suitable because carbon steel becomes brittle, elastomeric seals harden and crack, and conventional stem packing loses its sealing ability as the packing bore ices up with atmospheric moisture.

Extended-Stem (Cold-Box) Design

The defining feature of a cryogenic valve is the extended bonnet, also called a cold-box extension or cold stem. This extended neck keeps the packing gland and actuator at or close to ambient temperature, even when the valve body is immersed in liquid cryogen. The extended length is calculated to create a sufficient temperature gradient so that ice formation and packing damage in the gland area are prevented. Typical extension lengths range from 150 mm for LPG service at -50 degrees C to 600 mm or more for liquid helium at -269 degrees C.

Low-Temperature Material Qualification

MaterialMin. TemperatureCharpy Impact Test TempApplication
304/316 Austenitic Stainless Steel-196 C-196 C (no ductile-brittle transition)LNG, LPG, liquid N2, liquid O2
ASTM A352 LCB (Carbon Steel)-46 C-46 C (20 J minimum)LPG, propane, ethylene
ASTM A352 LC3 (3.5% Ni Steel)-101 C-101 C (20 J minimum)Ethylene, LPG at sub-ambient
9% Nickel Steel (ASTM A553)-196 C-196 C (34 J minimum)LNG storage, primary containment
Aluminium Alloy (5083)-196 CNot required (FCC crystal, ductile)LNG tanks, aluminium valve bodies
Hastelloy C-276-196 C-196 CCryogenic corrosive service

Seat and Seal Materials

Elastomeric seats based on NBR, EPDM, or neoprene are unsuitable for cryogenic service as they become glass-hard and fracture below -40 degrees C. Acceptable seat and seal materials include PTFE (usable to -200 degrees C), PCTFE (usable to -200 degrees C, preferred for oxygen service due to lower oxygen reactivity than PTFE), ultra-high-molecular-weight polyethylene (UHMWPE), and metal-to-metal seats in 316 SS or Stellite overlay for fire-safe and highest reliability applications. For liquid oxygen, all non-metallic materials must pass oxygen compatibility testing per ASTM G63 and G88.

Cryogenic Testing Requirements

  • BS 6364 (UK/International): the primary standard for cryogenic valves — specifies cold functional test at service temperature, shell and seat leakage at -196 degrees C, and cycling requirements
  • API 6D Annex F: cryogenic qualification testing for pipeline valves in LNG service
  • ASME B16.34: pressure-temperature ratings at cryogenic temperatures with separate tables for austenitic and low-alloy materials
  • Shell MESC SPE 77/300: extended-stem design and testing for Shell LNG projects
  • Cold functional test: valve must open and close smoothly after cold-soak at design temperature with internal cryogenic medium
  • External leakage test: packing gland must be leak-free (0.001 sccs helium maximum) at cryogenic temperature
  • Thermal cycling: typically 5 cycles from ambient to design temperature to verify no fatigue cracking

Valve Types for LNG Service

Valve TypeLNG ApplicationKey Design Feature
Cryogenic Ball ValveLNG transfer lines, loading arms, storage tank outletsExtended stem, PTFE seats, trunnion-mounted for large bore
Cryogenic Gate ValveLarge-bore main isolation, storage tank nozzle valvesExtended bonnet, OS&Y, bolted bonnet for easy maintenance
Cryogenic Globe ValveThrottling in LNG vaporisers, flow control on send-outExtended bonnet, PTFE packing, metal seat for fire-safe
Cryogenic Butterfly ValveLow-pressure LNG lines, vapour recovery systemsTriple-offset design, metal seat, cryogenic-rated PTFE
Cryogenic Check ValveAnti-reverse flow on pumps, compressors, vapour linesSpring-assisted swing or nozzle type with SS internals
Safety Relief Valve (SRV)LNG tank overpressure protection, boil-off gas linesStainless steel spring and disc, set pressure per ASME VIII Div.1

LNG Project Valve Specifications

Major LNG projects specify cryogenic valves to BS 6364 or API 6D Annex F with full PMI (positive material identification), radiographic or UT inspection of pressure-containing welds, and cold functional testing witnessed by third-party inspectors from Lloyd's, Bureau Veritas, or DNV. Extended stems are sized to maintain the packing above 0 degrees C in normal operating conditions. For safety-critical isolation duties, double-block-and-bleed (DBB) cryogenic ball valves with cavity vent are specified to prevent thermal expansion lock-up of trapped cryogenic liquid.

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