LNG & Cryogenic Service×Gate Valves

Gate Valves for LNG & Cryogenic Service

Cryogenic gate valves are used throughout LNG liquefaction trains, LNG storage and transfer, liquid nitrogen (LN₂), liquid oxygen (LOX), liquid argon (LAR), and ethylene plants where temperatures fall as low as –196°C for nitrogen service and –162°C for LNG. Vajra Industrial Solutions supplies low-temperature and cryogenic gate valves with ASTM A352 LCC/A350 LF2 bodies, extended bonnets, and testing to BS 6364 / ASTM B16.34 for LNG terminals, air separation units, and cryogenic chemical plants.

Key Applications — Gate Valves in LNG & Cryogenic Service

LNG Liquefaction Trains

Main cryogenic isolation on LNG rundown, storage tank inlet/outlet, and loading arms; Class 300–900 cryogenic gate valves in ASTM A350 LF2 or A352 LCC, tested to –196°C.

DN50–DN600 | Class 300–900 | A352 LCC / A350 LF2 | BS 6364, ASME B16.34

LNG Import/Export Terminals

Jetty unloading arm isolation, storage tank pump discharge, sendout pipeline isolation; large-bore cryogenic gate valves with actuators for remote ESD.

DN400–DN900 | Class 300–600 | A352 LCC / A350 LF2 | BS 6364, API 6D

Air Separation Units (ASU)

Liquid nitrogen, liquid oxygen, and liquid argon product isolation; cryogenic gate valves in SS 316L or A352 LCC with 100% radiographic weld inspection.

DN25–DN400 | Class 150–600 | SS 316L / A352 LCC | BS 6364, ASME B16.34

Ethylene / Ethane Plants

Cryogenic demethaniser and ethylene refrigeration circuit isolation; LCC body with A350 LF2 flanges for –100°C to –120°C ethylene service.

DN50–DN400 | Class 300–600 | A352 LCC + A350 LF2 | ASME B16.34, NACE MR0175

Cryogenic Truck / Rail Loading

Filling station isolation, breakaway protection, and excess flow protection in liquid gas loading stations for LN₂, LOX, and LAR.

DN25–DN150 | PN16–PN40 | SS 316L / A350 LF2 | BS 6364, EN 13480

Biomedical Gas Distribution

Medical-grade liquid nitrogen and oxygen distribution systems in hospital and research campus cryo-infrastructure.

DN15–DN100 | PN16–PN25 | SS 316L | BS 6364, ISO 7396-1 (medical gas)

Required Certifications

BS 6364 — British Standard for cryogenic valves: extended bonnet, vent/test valve, design and type testing at cryogenic temperatureASME B16.34 — pressure-temperature ratings, cryogenic service material (Table A1 low-temperature column)ASTM A352 Grade LCC (–46°C rated) or LCB (–46°C) for bodyASTM A350 Grade LF2 (–46°C) for forged flanges and bonnetsASTM A320 Grade L7 or B8M for cryogenic bolting (Charpy impact tested at –101°C)API 598 / BS 6755 seat testing at cryogenic temperature (helium or LN₂ medium test)

Recommended Materials

ASTM A352 LCC (cast) — carbon-manganese-molybdenum steel, Charpy impact tested at –46°C; standard body for LNG and –50°C to –160°C cryogenic service with proper design
ASTM A350 LF2 (forged) — normalized and tempered carbon steel, Charpy at –46°C; standard for cryogenic forged body gate valves
ASTM A182 F316L (forged stainless) — required for liquid oxygen service (LOX) and applications where carbon steel is not acceptable due to chemical compatibility (avoid austenitic SS for liquid hydrogen — use SS or Inconel per hydrogen embrittlement assessment)
ASTM A320 L7 (alloy steel bolting, –101°C) — standard bolting for cryogenic valve bonnets; B8M SS 316 bolting alternative for austenitic body valves

Selection Factors

Extended bonnet requirement: cryogenic gate valves must have an extended bonnet (per BS 6364) to keep the stem packing warm — the bonnet length ensures the packing gland remains above 0°C even when the valve body is at –162°C; BS 6364 specifies minimum bonnet length vs. operating temperature
Vent hole in bonnet / yoke: a 1/4" vent hole between the upper and lower seat (or in the bonnet) is required in cryogenic ball and gate valves to prevent trapped liquid from vaporising and creating hydraulic over-pressure when the valve is closed — verify that the valve design includes a vent hole or upstream-side cavity pressure relief per the service requirements
Impact testing: all pressure-retaining components (body, bonnet, body bolting) must have Charpy V-notch impact test results at the minimum design temperature; typically 27 J minimum at –46°C for LCC/LF2 material; higher impact energy required for Class 1 cryogenic service per BS 6364
End connection: raised-face (RF) flanges are acceptable for most LNG service; ring-type joint (RTJ) for high-pressure Class 600+ LNG service; butt-weld (BW) ends for permanent welded installations to minimize leak path count
Cleaning for oxygen service: all valves for LOX (liquid oxygen) service must be cleaned to ASTM G93 Level C or equivalent (oil-free, oxygen-compatible lubricants only); this is a safety-critical requirement — oxygen + hydrocarbon contamination = explosion hazard

Technical FAQs

Why does a cryogenic valve need an extended bonnet?
A cryogenic valve extended bonnet serves a critical function: it keeps the packing gland at or above ambient temperature while the valve body is at cryogenic temperature (–162°C for LNG, –196°C for LN₂). This is necessary because: (1) most packing materials (PTFE, graphite, soft elastomers) lose their sealing ability at cryogenic temperatures — they become brittle and rigid at –160 to –196°C and cannot maintain the compression and sealing contact needed to prevent leakage; (2) if condensation or atmospheric moisture freezes on the stem packing, the stem may bind (freeze-seized); (3) extended bonnet design creates a thermal gradient along the bonnet length — the valve body is at –162°C, but by the time the cryogenic fluid vapour rises through the bonnet column, it warms and the packing area stays above –20°C where standard PTFE packing remains effective. BS 6364 specifies the minimum bonnet length as a function of the test/operating temperature and the valve nominal size. The bonnet length for an LNG (–162°C) gate valve is significantly longer than for a –46°C low-temperature service valve. Always specify the operating temperature on your enquiry for cryogenic valves — the bonnet length is determined by this temperature, and bonnet length affects the overall installed height of the valve (critical for platform/vessel space planning).

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