Risk Analysis and Assessment of Butane-Propane Splitter Column in the Skikda Refinery Petroleum Plant

Amin Benaissa, Mohyiddine Hamaidia, Malika Khelfaoui, Wafia Benhamlaoui
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Abstract

Risk analysis and assessment are extremely important in the petrochemical sector to prevent potential risks. This study was carried out at Gas platform (unit No 30) of Skikda refinery Algeria, with the aim of predicting and estimating the effects of major explosions in the propane and butane Splitter column and estimating the possible human and environmental consequences of the containment loss. The methodology developed here is based on a combination of HAZOP presentation and PHAST tool. First, HAZOP is used to capture the responsible derivations of operating parameters to produce the worst consequences. Related Causes, safety barriers and some recommendations are carried out in a HAZOP sheet which represents all of that. Then the major scenarios detected by the worst consequences have been studied and modeled by PHAST software. The modeling process is completed by simulating the principal effects (Jetfire, BLEVE, UVCE) resulting from two scenarios in the form of two potential leaks on the bottom and the head of a gas separator column containing butane and propane respectively. The results are shown on the region map to indicate the exact threaten zones. Finally, a comparison in terms of effects between the two scenarios is performed and some conclusions are extracted.  
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斯基克达炼油厂丙烷裂解塔风险分析与评价
在石化行业中,风险分析和评估对于防范潜在风险至关重要。这项研究是在阿尔及利亚Skikda炼油厂的天然气平台(30号装置)进行的,目的是预测和估计丙烷和丁烷裂解塔发生重大爆炸的影响,并估计容器损失可能对人类和环境造成的后果。本文开发的方法是基于HAZOP表示和PHAST工具的结合。首先,HAZOP用于捕获产生最坏后果的操作参数的负责衍生。相关原因,安全屏障和一些建议在HAZOP表中进行,代表了所有这些。然后利用PHAST软件对最坏后果检测到的主要情景进行了研究和建模。建模过程通过模拟两种情况下的主要影响(Jetfire, BLEVE, UVCE)来完成,分别以含有丁烷和丙烷的气体分离器塔底和塔头两个潜在泄漏的形式进行。结果显示在区域地图上,以指示确切的威胁区域。最后,对两种方案的效果进行了比较,并得出了一些结论。
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