P&ID extraction for lng.
LNG facilities are SIS-dense by design. The cryogenic process is unforgiving, 2oo3 voting on critical services is routine, and proof-test cadence sits on a 6-12 month clock the audit register has to track.
- Per-unit I/O list, gas treatment, liquefaction trains, storage and loading
- Comprehensive SIS instrument index with SIL allocation references
- Cryogenic line list with metallurgy and insulation flags
- Custody-transfer metering scope filtered into a separate audit register
- Liquefaction trains carry redundant temperature, pressure, and level transmitters voting 2oo3. Redundancy annotations preserved
- Storage tank overfill protection, LSHH multi-layer, vented spill containment carries the facility's highest-SIL services
- Custody-transfer metering, Coriolis or USM carries weights-and-measures audit scope alongside controls scope. Both surface in the extraction
- Cryogenic service drives strict material specification. Line list preserves spec-break notation through the cold box
- Boil-off gas, BOG handling and reliquefaction loops add a dense instrumentation block tied to storage tank pressure control
- Marine loading arms, ship-shore communication, and ESD interfaces filter into a terminal-scope subset distinct from upstream process
- Liquefaction lineage, APCI, Cascade, Linde MFC, ConocoPhillips Optimized does not change I/O list output but affects parent equipment list and cold-box nomenclature
- Cryogenic relief and venting are heavily instrumented. PSV inlet and outlet temperature monitoring appears across multiple drawings
- IEC 61511, ISA 84. SIL allocation and proof-test discipline at the highest end of the spectrum
- API 625 for storage tank design
- USCG, US and equivalent maritime authorities for export terminal scope
- Custody-transfer metering audited under NIST Handbook 44 or international equivalents
Which discipline reads it.
Controls EngineerControls EngineersCryogenic instrumentation across liquefaction trains. Tank-farm and jetty signal scope.Process EngineerProcess EngineersCascade or mixed-refrigerant cycle balance. Cold-box stream summary integration with the recovery loop.Functional Safety EngineerFunctional Safety EngineersSIS scope on tank overfill, BOG compressor trip, and ESD network. LOPA per API 521 and NFPA 59A.Piping and Mechanical EngineerPiping and Mechanical EngineersCryogenic line classes, 9% nickel, austenitic stainless. Vacuum-insulated piping notation preserved.
TT-LN-1015-1oo2Liquefaction train 1 cold-box temperature, voted 1oo2LSHH-ST-302Storage tank 3 overfill switch, SIS-classified, segregated cabinetFT-CT-401Custody-transfer flow on the export berth manifoldMT-DH-205TEG dehydration outlet moisture analyzerPT-BOG-601-2oo3Boil-off gas header pressure, voted 2oo3ESDV-MLA-2-04Marine loading arm 2 emergency shutdown valve, position 04Related
GlossarySafety Instrumented System, SISGlossarySafety Integrity Level, SILGlossaryIEC 61511AudienceFor Controls EngineersAudienceFor Process EngineersAudienceFor Functional Safety EngineersAudienceFor Piping and Mechanical EngineersIndustryPetrochemicalsIndustryRefiningSolutionVerify SIS scope and SIL allocation against P&IDsSolutionP&ID revision comparisonConvertP&ID to I/O listConvertP&ID to instrument indexConvertP&ID to line list