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semi-quantitative protection layer analysis methodology protection analysis sil classification independent protection layer independent protection regularly typical protection layer failure probability appendix a b glossy coated paper matte coated paper kit scopethis document oxygen supply interface
GB/T 32857-2016 in English

GB/T 32857-2016 in English

SUPERSEDED

Application 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
Price(USD): $630.00
$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 dimensionsSpecific requirementsTypical 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

  1. Preferentially adopt intrinsically safe design to eliminate hazards
  2. For residual risks, at least two layers of independent protection
  3. Regularly verify the effectiveness of IPL (such as SIS functional testing)
  4. 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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