通过保护层分析(LOPA)对伊玛目-霍梅尼石化芳烃装置的设备进行定量评估

Pariya Sarafraz, K. Varshosaz, Neda Orak, Nematollah Jaafarzade, Ebrahim Aghajari
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摘要

背景:在石化行业,事故一般都是灾难性的,会危及人类、环境和经济。在这些行业中,有多种易燃和有毒物质会影响工人的健康和安全。它们还会对社会产生不利影响。数值风险和影响评估以及针对灾难性事件的保护层设计对于工艺装置的设计十分必要。方法:首先,通过危险与可操作性分析(HAZOP)和环境失效模式与影响分析(EFMEA)技术对职业-工艺和环境安全隐患进行测量。然后,使用层和可操作性分析 (LOPA) 方法对风险进行评估。结果显示结果表明,通过 HAZOP 和 EFMEA 方法,伊玛目霍梅尼石化芳烃装置共确定了 50 个安全与健康项目和 37 个环境风险。低、中、高风险项目分别为 17、19 和 14 个。结论这项研究表明,在分析保护层方面,LOPA 方法比危险识别方法更全面。重要的行动是堵住通向火炬的过量气体和释放 H2S 气体。此外,对芳烃装置活动的环境评估表明,供电装置的空气污染物产生、反应器储罐的废物处置、冷凝液储罐的废物处置以及反应器的火灾和爆炸属于高风险级别。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Quantitative Evaluation by Protection Layer Analysis (LOPA) for Equipment in Imam Khomeini Petrochemical Aromatic Unit
Background: In the petrochemical industries, accidents are generally catastrophic which endanger human, environment and economic. In the industries, there is a wide range of flammable and toxic substances that affect health and safety of workers. They have also adverse effects on society. Numerical risk and impact assessment as well as design for protective layers against catastrophic events are necessary for designing process units. Methods: First, the occupational-process and environmental safety hazards were measured by hazard and operability (HAZOP) and environmental failure mode and effects analysis (EFMEA) techniques. Then, the risk was assessed using the layer and operability analysis (LOPA) method. Results: The results showed that a total of 50 safe and health items and 37 environmental risks were identified by HAZOP and EFMEA methods in Imam Khomeini Petrochemical Aromatic Unit. There were 17, 19 and 14 items with low, medium and high level risk, respectively. Conclusion: This study showed that the LOPA method is more comprehensive than hazard identification methods for the analysis of protective layers. The important actions were blockage of the excess gas to the flare and release the H2S gas. Also, evaluation of the environmental aspects of aromatic unit activities showed that air pollutant production in the power supply unit, waste disposal of reactor tank, waste disposal of condensate tank and reactor fire and explosion were at a high level risk.
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