Simulated Annealing Approach to the Optimal Synthesis of Distillation Column with Intermediate Heat Exchangers

This article presents a simulated annealing-based approach to the optimal synthesis of distillation column considering intermediate heat exchangers arrangements. T-he number of intermediate condensers and/or intermediate reboilers, the placement locations, the.operating pressure of column, and the h...

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Published inChinese journal of chemical engineering Vol. 16; no. 1; pp. 30 - 35
Main Author 安维中 于凤娟 董凤蕾 胡仰栋
Format Journal Article
LanguageEnglish
Published Elsevier B.V 01.02.2008
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ISSN1004-9541
2210-321X
DOI10.1016/S1004-9541(08)60031-2

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Abstract This article presents a simulated annealing-based approach to the optimal synthesis of distillation column considering intermediate heat exchangers arrangements. T-he number of intermediate condensers and/or intermediate reboilers, the placement locations, the.operating pressure of column, and the heat duties of intermediate heat exchangers are treated as optimization variables. A novel coding procedure making use of an integer number series is proposed to represent and manipulate the structure of system and a stage-to-stage method is used for column design and cost calculation. With the representation procedure, the synthesis problem is formulated as a mixed integer nonlinear programming (MINLP) problem, which can then be solved with an improved simulated annealing algorithm. Two examples are illustrated to show the effectiveness of the suggested approach.
AbstractList This article presents a simulated annealing-based approach to the optimal synthesis of distillation column considering intermediate heat exchangers arrangements. T-he number of intermediate condensers and/or intermediate reboilers, the placement locations, the.operating pressure of column, and the heat duties of intermediate heat exchangers are treated as optimization variables. A novel coding procedure making use of an integer number series is proposed to represent and manipulate the structure of system and a stage-to-stage method is used for column design and cost calculation. With the representation procedure, the synthesis problem is formulated as a mixed integer nonlinear programming (MINLP) problem, which can then be solved with an improved simulated annealing algorithm. Two examples are illustrated to show the effectiveness of the suggested approach.
This article presents a simulated annealing-based approach to the optimal synthesis of distillation column considering intermediate heat exchangers arrangements. The number of intermediate condensers and/or intermediate reboilers, the placement locations, the operating pressure of column, and the heat duties of intermediate heat exchangers are treated as optimization variables. A novel coding procedure making use of an integer number series is proposed to represent and manipulate the structure of system and a stage-to-stage method is used for column design and cost calculation. With the representation procedure, the synthesis problem is formulated as a mixed integer nonlinear programming (MINLP) problem, which can then be solved with an improved simulated annealing algorithm. Two examples are illustrated to show the effectiveness of the suggested approach.
Author 安维中 于凤娟 董凤蕾 胡仰栋
AuthorAffiliation Department of Chemical Engineering, Ocean University of China, Qingdao 266100, China
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Cites_doi 10.1002/aic.690440609
10.1021/ie50269a005
10.1126/science.220.4598.671
10.1021/ie9601312
10.1016/S0098-1354(97)00015-X
10.1002/aic.690431111
10.1002/aic.690440608
10.1021/ie040178k
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Keywords intermediate heat exchanger
synthesis
mixed integer nonlinear programming
simulated annealing
distillation
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Snippet This article presents a simulated annealing-based approach to the optimal synthesis of distillation column considering intermediate heat exchangers...
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SubjectTerms distillation
intermediate heat exchanger
mixed integer nonlinear programming
simulated annealing
synthesis
中间换热器
优化综合
模拟退火方法
精馏塔
Title Simulated Annealing Approach to the Optimal Synthesis of Distillation Column with Intermediate Heat Exchangers
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