GB/T 32857-2016 in English
SUPERSEDEDApplication guide for layer of protection analysis(LOPA)
- Issued on:2016-08-29
- Implemented on:2017-03-01
- File Format:PDF
- Delivery:Via email within 5 business days
$612.00
《GB/T 32857-2016保护层分析(LOPA)应用指南》由TC124(全国工业过程测量控制和自动化标准化技术委员会)归口,主管部门为中国机械工业联合会。
Introduction
Analysis of the core content of the standard
GB/T 32857-2016, as an important standard for process industry safety risk assessment, proposes a semi-quantitative protection layer analysis methodology. Its core value lies in:
- Establish a complete scenario chain from initial events to consequences
- Quantitatively evaluate the effectiveness of existing protection measures
- Provide technical basis for SIL classification
Independent Protection Layer (IPL) determination framework
| Determination dimensions | Specific requirements | Typical examples |
|---|---|---|
| Effectiveness | Ability to detect anomalies in time and execute safety actions | Safety Instrumented System (SIS) temperature high interlock |
| Independence | No common cause failure with initial events and other IPLs | Emergency pressure relief valve independent of BPCS |
| Auditability | Performance can be verified through testing | Records of periodic calibration of safety valves |
Reference for typical protection layer failure probability
Appendix A of the standard provides the PFD benchmark values widely recognized by the industry:
- Basic process control loop (BPCS): 10-2~10-1
- Operator intervention (10 minute response): 10-1~100
- SIL1 safety instrumented function: 10-2~10-1
- Mechanical safety valve: 10-5~10-1
Note: The actual value needs to be adjusted in combination with the service conditions and maintenance level of the equipment
Implementation suggestions
- Preferentially adopt intrinsically safe design to eliminate hazards
- For residual risks, at least two layers of independent protection
- Regularly verify the effectiveness of IPL (such as SIS functional testing)
- Use the LOPA record sheet provided by the standard to standardize the analysis process
A typical case shows that in the scenario of temperature runaway of the polymerization reactor, the risk frequency can be reduced from 10-2/year to 10-5/year by adding a SIL2 interlock system.

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