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Piping & Fittings

Hydrogen Piping — ASME B31.12

ASME B31.12 piping & pipelines for hydrogen service (gaseous, liquid).

Category
Piping & Fittings
Subcategory
Specialty Piping
Applicable standards
3
Issuing bodies
1

Description

ASME B31.12 piping & pipelines for hydrogen service (gaseous, liquid).

Applicable Standards (3)

ASME — 3 standards

ASME B31.12 Hydrogen Piping and Pipelines
Edition: 2023 Edition Region: USA, Global
Industrial piping (Part IP) and pipelines (Part PL) for gaseous and liquid hydrogen, including hydrogen embrittlement controls.
ASME B31.3 Process Piping
Edition: 2022 Edition Region: USA, Global
Piping in petroleum refineries; chemical, pharmaceutical, textile, paper, ore-processing plants and related processing facilities. Default process piping code worldwide.
Key requirements (10)
  • Process piping — refining, chemical, pharmaceutical, semiconductor.
  • Categories: Normal Fluid Service (default), Category D (low pressure < 150 psig & temp 38–186 °C), Category M (lethal), High Pressure, Severe Cyclic, High Purity.
  • Allowable stress: lower of UTS/3, Yield/1.5, etc., from Table A-1.
  • Wall thickness: t = P·D / (2·(S·E·W + P·Y)) where Y = 0.4 for ductile under 482 °C.
  • Joint efficiency E: 1.0 (seamless), 0.85–0.95 (welded depending on RT).
  • Hydrotest: 1.5 × design pressure × (S_test/S_design) — ≥ 10 minutes hold.
  • Pneumatic test (when hydro impractical): 1.1 × design pressure with safety analysis.
  • Examination: 5% RT for Normal service; 100% RT for Category M and Severe Cyclic.
  • Flexibility analysis required when temperature differential > 28 °C and complex routing.
  • Stress range allowable SA = f·(1.25·Sc + 0.25·Sh) with f = cyclic reduction factor.
ASME B31.8 Gas Transmission and Distribution Piping Systems
Edition: 2022 Edition Region: USA, Global
Pipelines transporting natural and other gases.
Key requirements (7)
  • Gas transmission and distribution piping.
  • Class locations 1–4 based on population density within 1/4-mile (200 ft typical x 1 mi each side of pipeline).
  • Design factor F: 0.72 (Class 1 Div 2), 0.60 (Class 2), 0.50 (Class 3), 0.40 (Class 4).
  • Hydrotest: typical 1.25 × MAOP for 8 hours minimum.
  • MAOP = 2·S·t·F·E·T/D — basis for design.
  • Compressor stations covered per Chapter VIII (B31.8); offshore per B31.8.S.
  • Pipeline integrity management per ASME B31.8S (gas) — covers HCAs (high consequence areas).