Pre-selection for industrial process valves

Valves for LNG and Cryogenic Service

−162 °C is past this tool's data boundary — and we say so

LNG duty at −162 °C sits below this tool's −46 °C floor, and the reason is data, not doubt about capability. Cryogenic valve selection is its own discipline — extended bonnets sized by rule, cold-box layout, drip plates, and a dedicated low-temperature type-test regime (the successor to BS 6364). None of that layer is in our knowledge base, so the tool refuses rather than approximates.

The capability itself is proven — including by Chinese makers, whose delivered cryogenic valves this site has reported. The boundary is that the published selection data does not exist in a form we can put in a table. Duties like this go to our engineering-review channel, and we confirm them by hand.

Typical duties

LNG carrier and terminal isolation≈ −162 °C · cryogenic design · outside the automatic envelope
Cold-box and liquefaction-train valvingCold-box layout and drip plates are design questions, not catalogue rows
High-pressure cryogenic controlReported in the field at −130 °C / Class 2500 — see the award below
Engineering review, by design

This application sits outside the tool's data boundary — the reason is stated above, not hidden. Send the duty through the inquiry channel and a manufacturer's engineering team confirms it by hand.

Open the selector → (the form's engineering-review path applies)

What to watch

  • This page deliberately runs no demo: every honest answer here is an engineered one.
  • The old British cryogenic standard was withdrawn in 2015 — the linked article covers what a specification should name instead.
  • China's own low-temperature valve test standard (GB/T 24925) is covered in a companion piece.

Where this connects on this site

Boundary rule: this page states single-point conclusions from the site's knowledge base — no supplier names, no matrices. The full 40-medium library lives in the selector.