Instrumentation & Control Design Guide
Chapter from the Instrumentation & Control Design Guide.
| SIL Level | PFD Range | Risk Reduction Factor | Availability | Typical Application | Architecture | Testing Interval |
|---|---|---|---|---|---|---|
| SIL 1 | 0.01-0.1 | 10-100 | 90-99% | Most refinery SIFs | 1oo1 or 1oo2 | Annual |
| SIL 2 | 0.001-0.01 | 100-1,000 | 99-99.9% | High-consequence SIFs | 1oo2 or 2oo3 | Semi-annual to annual |
| SIL 3 | 0.0001-0.001 | 1,000-10,000 | 99.9-99.99% | Catastrophic prevention | 2oo3 or 2oo4 | Quarterly to semi-annual |
| SIL 4 | 0.00001-0.0001 | 10,000-100,000 | 99.99%+ | Not typical in refining | Highly redundant | Not typical in process industry |
1. Hazard & Risk Assessment: HAZOP, LOPA → identify SIF requirements
2. SIL Determination: LOPA or risk graph → assign SIL to each SIF
3. Safety Requirements Specification (SRS): document each SIF
• Process variables monitored
• Final element action (de-energize to trip, fail-safe direction)
• Required PFD and SIL
• Proof test interval
• Response time requirement
4. SIS Design: select sensors, logic solver, final elements
• Voting architecture: 1oo1, 1oo2, 2oo3
• Diagnostics coverage
• Common cause failure analysis
5. SIL Verification: calculate achieved PFD
• Include sensor, logic solver, and final element failure rates
• Account for proof test interval, diagnostic coverage, common cause
6. Factory Acceptance Test (FAT)
7. Commissioning & Validation
8. Operation & Maintenance: proof testing per SRS
Source: Instrumentation_Control_Design_Guide_v1.xlsx · sheet “SIS Design”
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