Chemical and Process Inherent Safety Analysis of Large-Scale Suspension Poly(Vinyl Chloride) Production

IF 2.8 Q2 ENGINEERING, CHEMICAL ChemEngineering Pub Date : 2023-08-24 DOI:10.3390/chemengineering7050076
Á. González-Delgado, Eduardo Aguilar-Vásquez, Miguel Ramos-Olmos
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引用次数: 1

Abstract

In this work, a safety assessment was carried out for the suspension polymerization method, known for the lack of studies about its sustainable performance and long history of chemical accidents. Therefore, a safety analysis was conducted using the inherent safety methodology to assess and determine the inherent risks of the poly(vinyl chloride) (PVC) suspension production process using computer-aided process engineering (CAPE). The indicators were calculated using data from safety databases and the specialized literature, considering downstream stages like vinyl chloride monomer (VCM) recovery, PVC purification and PVC drying. The obtained indicators revealed that the process has a negative performance regarding inherent safety, with a total inherent safety index of 30. The chemical inherent safety index had a value of 19, with the main chemical risk of the process being presented by the vinyl chloride monomer (with a value of 11), along with the risk of the exothermic reactions. The process safety index had a value of 15, highlighting the inventory as the primary concern of the process (with a value of 5), followed by the presence of unsafe equipment such as furnaces, burners, and dryers. The safety structure index had a score of 3, categorizing the process as probably risky, with the reaction and purification stages being more susceptible to accidents. Lastly, it is recommended to reduce the size of the process inventory and to substitute out unsafe process units.
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大规模悬浮聚氯乙烯生产的化学和工艺固有安全性分析
在这项工作中,对悬浮聚合方法进行了安全评估,该方法因缺乏对其可持续性能的研究和长期的化学事故历史而闻名。因此,使用固有安全方法进行了安全分析,以使用计算机辅助工艺工程(CAPE)评估和确定聚氯乙烯(PVC)悬浮液生产过程的固有风险。这些指标是使用安全数据库和专业文献中的数据计算的,考虑到氯乙烯单体(VCM)回收、PVC纯化和PVC干燥等下游阶段。所获得的指标表明,该工艺在固有安全方面具有负面表现,总固有安全指数为30。化学固有安全指数的值为19,氯乙烯单体(值为11)以及放热反应的风险是该工艺的主要化学风险。工艺安全指数的值为15,突出表明库存是工艺的主要问题(值为5),其次是存在不安全的设备,如熔炉、燃烧器和干燥器。安全结构指数得分为3,将该过程归类为可能有风险,反应和纯化阶段更容易发生事故。最后,建议减少工艺库存的规模,并替换不安全的工艺单元。
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来源期刊
ChemEngineering
ChemEngineering Engineering-Engineering (all)
CiteScore
4.00
自引率
4.00%
发文量
88
审稿时长
11 weeks
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