石油化工安全环保技术 ›› 2024, Vol. 40 ›› Issue (2): 28-32.

• 安全与环保设计 • 上一篇    下一篇

天然气管道周边区域个人风险计算分析

齐先志1,王静静2,王晓霖1,李明1,奚旺1   

  1. 1. 中石化(大连)石油化工研究院有限公司,辽宁 大连 116045 ;
    2. 河南省中友石油天然气技术服务公司济南分公司,山东 济南 250014
  • 收稿日期:2022-12-07 接受日期:2024-03-15 出版日期:2024-04-20 发布日期:2024-04-24
  • 作者简介:齐先志,男,工程师,2012 年硕士毕业于北京化工大学材料科学与工程专业,现主要从事油气管道完整性管理和风险评价方向的研究工作。电话:15804112025,E-mail :qixianzhi1986@126.com。

Individual Risk Calculation and Analysis in the Vicinity of Gas Transmission Pipeline

Qi Xianzhi1,Wang Jingjing2,Wang Xiaolin1,Li Ming1,Xi Wang1   

  1. 1. SINOPEC (Dalian) Petrochemical Research Institute Co., Ltd., Dalian, Liaoning, 116045;
    2. Jinan Branch of Henan Zhongyou Oil & Gas Technology Services Limited, Jinan, Shandong, 250014
  • Received:2022-12-07 Accepted:2024-03-15 Online:2024-04-20 Published:2024-04-24

摘要: 为了分析输气管道周边区域风险水平,建立了个人风险计算模型。该模型包括管道失效频率计算和失效危害后果计算两部分内容。该模型将管道失效原因分为6 类,采用修正基准频率的方法计算每类失效原因造成的管道失效频率;危害后果计算分析包括:泄漏速率计算、引燃概率计算分析、火灾计算分析和伤害程度,采用喷射火表征管道泄漏危害后果。在失效频率和泄漏后果计算分析的基础上,计算管道周边区域的个人风险,明确风险是否可接受。风险计算实例表明,破裂是构成风险的主要因素,建议强化对破裂诱发因素的管控。

关键词: 个人风险, 失效频率, 输气管道, 喷射火

Abstract: In order to analyze the risk in the vicinity of the gas transmission pipeline, an individual risk calculation model is established. The model consists of two parts involving the calculation of pipeline failure frequency and the calculation of the hazardous consequences of failure. The model divides the causes of pipeline failure into six categories. The method of correcting the reference frequency is adopted to calculate the frequency of pipeline failure caused by each category of the failure causes. The calculation and analysis of hazardous consequences include four parts covering leakage rate calculation, calculation and analysis of ignition probability, fire calculation and analysis, and degree of injury. Jet fire is used to represent the hazardous consequences of pipeline leakage. Based on the calculation and analysis of the failure frequency and leakage consequences, the individual risk in the vicinity of the pipeline is calculated. Thus, whether the risk in the vicinity of pipeline is acceptable or not can be determined. Examples of risk calculation show that rupture is the main factor for risk, and it is recommended that the control of rupture-inducing factors should be strengthened.

Key words: individual risk, failure frequency, gas pipeline, jet fire