The identification and analysis of risks in Hydrogen unit of refinery using HAZOP and LOPA techniques

A. Delavar, M. Tehrani, Seyed Shamseddin Alizadeh
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引用次数: 0

Abstract

Process industries have always been exposed to fire, explosion and release of chemical materials. To identify and evaluate risk in process industries including oil and gas, there are various methods in which hazard and operability study (HAZOP) is one of the most common methods. To do this, at first all organizational duties and unit activities are identified. Then, the study technique of operation and risk is used as an effective and sys thematic method to identify risk and operating problems and the relevant effects. The identified activities in risk assessment are applied. The results of evaluation of identified risks showed that 6 cases had hazard higher than 15 and it is not acceptable. In terms of risk intensity, the highest frequency of unacceptable risks (4 cases) is observed in “reformer heating chamber”.  The analysis of consequence of hazards showed that for 6 hazardous points, independent layers of protection can reduce risk as 100% to target factor (10 -5 ) and safety integrity level is fulfilled completely.
运用HAZOP和LOPA技术对炼油厂氢气装置进行风险识别和分析
过程工业一直暴露在火灾、爆炸和化学物质释放的环境中。为了识别和评估包括石油和天然气在内的过程工业中的风险,有多种方法,其中危害和可操作性研究(HAZOP)是最常用的方法之一。为此,首先要确定所有组织职责和单位活动。然后,将经营与风险研究技术作为一种有效的、系统的专题方法来识别风险与经营问题及其影响。应用风险评估中确定的活动。对已识别风险的评价结果显示,6例的危险度高于15,是不可接受的。在风险强度方面,“重整炉加热室”出现不可接受风险的频率最高(4例)。危害后果分析表明,对于6个危险点,独立防护层可将风险降低至目标因子(10 -5)的100%,完全达到安全完整性等级。
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