π Case Study
Offshore LNG Transfer System Fault Tree Analysis and SIS Architecture Optimization
High consequence of LNG spill + ignition in congested maritime corridor; existing SIS used single-channel logic
ποΈ Project Overview
FPSO-based LNG bunkering operation in Singapore Strait
π― Challenge
High consequence of LNG spill + ignition in congested maritime corridor; existing SIS used single-channel logic
π§ Design Approach
Top-down fault tree for 'uncontrolled LNG release' initiating event; redesigned SIS to 2oo3 voting architecture with diverse sensors (radar + Coriolis + ultrasonic), certified per IEC 61511 SIL 3
π Design Diagram
AI-generated project design illustration
π Key Calculations
PFDavg
Ξ»DU Γ TPT / 2 + Ξ»DD Γ Ξ²
Result: 1.2Γ10β»Β³
Confirmed SIL 3 capability
Common Cause Failure Beta Factor
Ξ² = (PFD_system β PFD_independent) / PFD_system
Result: 0.042
Guided sensor diversity specification
π Results
PFDavg improved from 2.8Γ10β»Β² to 1.2Γ10β»Β³; system availability increased from 92% to 99.4%; accepted by DNV GL Class and MPA Singaporeπ‘ Lessons Learned
- β’Fault tree depth must extend to maintenance errors and calibration drift
- β’Sensor diversity requires independent failure modesβnot just different technologies
- β’TPT extension beyond manufacturer recommendation increases spurious trip risk
β Key Takeaways
- 1Fault tree depth must extend to maintenance errors and calibration drift
- 2Sensor diversity requires independent failure modesβnot just different technologies
- 3TPT extension beyond manufacturer recommendation increases spurious trip risk
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Updated: 2026-07-20
Reviewed by: ToolFusion Engineering Team