LNG & Cryogenic×Ball Valves

Ball Valves for LNG & Cryogenic

LNG and cryogenic ball valves operate at temperatures down to −196°C (liquid nitrogen) and −162°C (LNG), demanding extended bonnet construction to prevent stem packing from reaching cryogenic temperatures, low-temperature impact-tested materials (SS 316L, A182 F304L, A350 LF2), and full live-loaded packing assemblies. Vajra Industrial Solutions supplies BS 6364-compliant cryogenic ball valves for LNG terminal block valves, loading arm isolation, LNG carrier manifold valves, and liquid nitrogen / liquid oxygen distribution systems — with API 6D certification for pipeline service and full EN 10204 3.2 documentation.

Key Applications — Ball Valves in LNG & Cryogenic

LNG Terminal Block Valves (Loading and Unloading)

Trunnion-mounted full-bore ball valves for LNG terminal loading and unloading headers. API 6D certified, full-bore design for maximum flow capacity and pigging. Extended bonnet prevents packing failure at −162°C LNG temperature. Fire-safe per API 607. Stainless steel 316L body and trim — no low-alloy steel (risk of brittle fracture at cryogenic temperatures).

DN50–DN600, Class 150–600, SS 316L, extended bonnet, API 6D, BS 6364, −162°C

Loading Arm Isolation and Emergency Disconnection

Manual and pneumatically actuated ball valves for LNG ship-to-shore loading arm isolation. Cryogenic extended bonnet with finned radiator section. Emergency shut-off (ESO) valves with spring-return pneumatic actuator for automatic closure on ESD system activation. Fire-safe API 607. All valves cryogenic impact tested to −196°C per BS 6364.

DN100–DN400, Class 150–300, SS 316L, pneumatic spring-return, API 607, BS 6364

LNG Storage Tank Outlet and Pump Suction

Bottom-entry cryogenic ball valves for LNG above-ground storage tank outlet connections and submerged pump suction lines. Bottom-entry design allows in-line seat replacement without removing valve from tank. A182 F304L forged body (ASTM A182 Grade F304L — low carbon SS 304L forged — maintains impact toughness to −196°C). Live-loaded stem packing for thermal cycling.

DN50–DN300, Class 150–300, A182 F304L forged, bottom-entry, live-loaded packing

Liquid Nitrogen and Liquid Oxygen Distribution

Cryogenic ball valves for industrial gas facilities handling liquid nitrogen (LN₂, −196°C), liquid oxygen (LOX, −183°C), and liquid argon (LAr, −186°C). Extended bonnet standard. A350 LF2 (low temperature carbon steel, Charpy-tested to −46°C) or SS 316L for LOX service. Oxygen cleaning (degreased and sealed) mandatory for LOX service — no hydrocarbon contamination permitted.

DN15–DN200, Class 150–600, SS 316L / A350 LF2, oxygen-cleaned for LOX, BS 6364

Cryogenic Piping Isolation — Instrument and Sample Connections

Small bore forged cryogenic ball valves for instrument root valves, cryogenic sampling connections, and vent and drain valves on LNG piping. DBB (Double Block and Bleed) design for safe sampling isolation. A182 F316L forged body, extended bonnet, socket weld or butt weld connections for orbital welding in LNG piping systems.

DN15–DN50, Class 800–1500, A182 F316L forged, extended bonnet, SW/BW ends, DBB option

Required Certifications

BS 6364 — Valves for Cryogenic Service (mandatory cryogenic testing standard)API 6D — Pipeline Ball Valves (LNG terminal mainline service)API 607 — Fire Testing (all hydrocarbon and LNG service)EN 10204 3.2 MTCs (third-party witnessed material certification for LNG)API 598 — Production Pressure Testing including low-temperature seat testATEX (actuated valves in LNG terminal hazardous area)ISO 21457 (materials selection for LNG systems — informative reference)

Recommended Materials

A182 F304L (SS 304L forged) — primary cryogenic ball valve body and trim material
A182 F316L (SS 316L forged) — for chloride-containing environments and marine LNG service
A351 CF8 / CF8M (SS 304/316 cast) — large bore cast body option
A350 LF2 (low temperature carbon steel) — LNG service down to −46°C; not for LN₂
PTFE (modified) or PCTFE seat — maintains elasticity at cryogenic temperatures
Inconel 625 (N06625) — trim overlay for wear resistance in high-velocity LNG

Selection Factors

Extended bonnet length: calculate per BS 6364 — bonnet must be long enough to keep packing above −29°C even when body is at −196°C
Material: All body and trim materials must pass Charpy V-notch impact testing at design temperature per BS 6364 / ASME B16.34
Bore: Full-bore mandatory for LNG terminal mainline (API 6D pigging requirement)
Fire-safe: API 607 certification required for all LNG service ball valves
Live-loaded packing: Required for thermal cycling service — LNG loading arms cycle between ambient and −162°C repeatedly
LOX service: Oxygen compatibility and cleaning per ASTM G93 / CGA G-4.1 mandatory — all hydrocarbon lubricants and sealants prohibited

Technical FAQs

What is BS 6364 and why is it required for cryogenic ball valves?
BS 6364 is the British Standard specification for valves for cryogenic service. It defines the minimum requirements for design, materials, testing, and marking of valves intended for service at temperatures below −10°C (including LNG at −162°C, liquid nitrogen at −196°C, and liquid oxygen at −183°C). The key requirements of BS 6364 are: (1) Cryogenic impact testing of all body and trim materials at the valve's minimum design temperature; (2) Extended bonnet construction — the bonnet must be long enough to maintain packing temperature above −29°C (the temperature at which most packing materials lose effectiveness); (3) Cryogenic functional test — every valve must be tested at cryogenic temperature with the medium it will handle (LN₂ or liquid helium bath) to verify seat tightness and operability at temperature; (4) Anti-static provision (earthing of ball to body). BS 6364 is cited in LNG terminal engineering specifications worldwide and is the dominant cryogenic valve testing standard. Valves not tested per BS 6364 are generally not accepted for LNG terminal or cryogenic industrial gas service.
Why is an extended bonnet necessary on cryogenic ball valves?
Cryogenic ball valves have an extended bonnet (elongated neck between the body and the actuator/handwheel) for a specific thermal reason: the stem packing (PTFE or graphite) becomes rigid and ineffective at cryogenic temperatures (below −30°C approximately). If the packing were located at the body (at −162°C or −196°C), it would leak or become impossible to adjust. The extended bonnet creates a thermal gradient along the stem — the body is at cryogenic temperature but the packing sits at the top of the bonnet where the temperature has risen (by conduction through the stem and convection along the bonnet exterior) to above −29°C, where PTFE packing remains functional. The length of the bonnet is calculated using heat conduction equations to ensure the packing temperature stays above the minimum functional temperature even at the minimum process temperature. Live-loaded springs on the packing gland compensate for PTFE cold-flow (permanent deformation under load at temperature) that would otherwise cause stem leakage during temperature cycling.
What is the difference between LNG service and LN₂ service for ball valves?
LNG (liquefied natural gas) service is at −162°C and involves a flammable hydrocarbon fluid — fire-safe design per API 607 is mandatory, and all materials and fabrication must prevent brittle fracture. LN₂ (liquid nitrogen) service is at −196°C — 34°C colder than LNG — and requires materials and design tested to −196°C. The lower temperature of LN₂ is the more demanding requirement. However, LN₂ is inert (non-flammable, non-toxic) so fire-safe design is not required. LOX (liquid oxygen, −183°C) adds the additional requirement of oxygen compatibility — all materials, lubricants, sealants, and cleaning agents must be verified safe for oxygen service (oxygen-incompatible materials can ignite in the presence of high-pressure LOX). A ball valve suitable for LNG service must be re-tested and oxygen-cleaned before it can be used in LOX service.

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