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Design Optimization of a Crude Oil Distillation Process
Author(s) -
Seo J. W.,
Oh M.,
Lee T. H.
Publication year - 2000
Publication title -
chemical engineering and technology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.403
H-Index - 81
eISSN - 1521-4125
pISSN - 0930-7516
DOI - 10.1002/(sici)1521-4125(200002)23:2<157::aid-ceat157>3.0.co;2-c
Subject(s) - distillation , operating cost , capital cost , fractionating column , process (computing) , nonlinear programming , process engineering , tray , optimal design , work (physics) , engineering , energy consumption , mathematical optimization , nonlinear system , computer science , mathematics , waste management , mechanical engineering , chemistry , physics , electrical engineering , organic chemistry , quantum mechanics , machine learning , operating system
In this work, the optimal design of a crude oil distillation unit was made. Since the method used here is based on the general optimization framework, it is possible to design the process systematically. The results of this study gave better performances than that of the existing process. The process in this study is currently in operation and has the capacity of 150,000 BPSD. Feed locations, heat duties of pumparounds and operating conditions of the preheat train are selected as variables, and the energy consumption, operating cost and annual cost are formulated as objective functions. The optimal feed locations of both the main column and stabilizer are obtained by solving rigorous models and mixed integer nonlinear programming. Considering the results of the optimal feed tray, the cost optimization is carried over to obtain the optimal annual cost, which considers both the capital and operating cost, which is decreased from US$10,649,000/year to USdollar;9,185,230/year.