Sustainable process design for heat exchanger network considering inherent safety and process economics

Muhammad Athar, A. M. Shariff, Muhammad Imran Rashid, Mahboob Ahmed Aadil, Asim Umer, Muhammad Irfan
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Abstract

Process lifecycle has several stages, including process design covered in multiple stages. Process economics is a vital factor in finalizing the process design. Besides economics, inherent safety is an important concept contributing to sustainable process design generation. The inherent safety concept has been applied via equipment characteristics for individual equipment. Since a method considering inherent safety with equipment aspects and process economics has not been available, therefore, a new method has been proposed, namely sustainable process design for heat exchanger network (SPDHEN), to integrate inherent safety, equipment aspects, and process economics. SPDHEN uses indexing to identify the critical heat exchanger, which is then examined via hazard analysis for an explosion. For unacceptable hazards, inherent safety principles are engaged to generate design alternatives for which process economics is examined too. The final design would be inherently safer with the best profit margin. The proposed method has been studied for the ammonia synthesis loop. It is concluded that the explosion hazard has been reduced to a tolerable level by using inherent guide words with a marginal compromise on quantity of ammonia produced, that is, 0.32%. This method is straightforward and can be useful for process engineers to generate sustainable process designs for heat exchanger networks considering safety and process economics simultaneously.
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考虑到固有安全性和工艺经济性的热交换器网络可持续工艺设计
工艺生命周期分为多个阶段,其中包括分多个阶段进行的工艺设计。工艺经济性是最终确定工艺设计的重要因素。除了经济性,固有安全性也是有助于产生可持续工艺设计的一个重要概念。固有安全概念是通过单个设备的设备特性来实现的。由于目前还没有一种将固有安全性与设备特性和工艺经济性结合起来考虑的方法,因此我们提出了一种新方法,即换热器网络可持续工艺设计(SPDHEN),将固有安全性、设备特性和工艺经济性结合起来。SPDHEN 采用索引法确定关键换热器,然后通过爆炸危险分析对其进行检查。对于不可接受的危险,则采用固有安全原则来生成设计替代方案,并对其工艺经济性进行检查。最终的设计将是本质上更安全且利润率最高的。针对氨合成回路研究了所提出的方法。结论是,通过使用固有的指导原则,爆炸危险已降低到可容忍的水平,但氨的生产量却略有下降,仅为 0.32%。这种方法简单明了,可帮助工艺工程师为热交换器网络进行可持续工艺设计,同时考虑安全性和工艺经济性。
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