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

被引:3
作者
Athar, Muhammad [1 ,2 ,3 ,6 ]
Shariff, Azmi Mohd [2 ,3 ]
Rashid, Muhammad Imran [4 ]
Aadil, Mahboob Ahmed [1 ]
Umer, Asim [1 ]
Irfan, Muhammad [5 ]
机构
[1] Muhammad Nawaz Sharif Univ Engn & Technol, Dept Chem Engn, Multan, Pakistan
[2] Univ Teknol PETRONAS, Ctr Adv Proc Safety CAPS, Seri Iskandar, Perak, Malaysia
[3] Univ Teknol PETRONAS, Chem Engn Dept, Seri Iskandar, Perak, Malaysia
[4] Univ Engn & Technol, Dept Chem Polymer & Composite Mat Engn, New Campus, Lahore, Pakistan
[5] Pakistan Council Sci & Ind Res PCSIR, Ctr Environm Protect Studies CEPS, Labs Complex, Lahore, Pakistan
[6] Muhammad Nawaz Sharif Univ Engn & Technol, Dept Chem Engn, Multan 60000, Pakistan
关键词
heat exchanger network; inherent safety; process design; process economics; sustainable; MULTIOBJECTIVE OPTIMIZATION; STORAGE FACILITIES; GRAPHICAL-METHOD; TOOL; INDEX; INTEGRATION; ACCIDENT;
D O I
10.1002/cjce.25202
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
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.
引用
收藏
页码:2481 / 2494
页数:14
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