A generalized distillation network synthesis model

被引:8
|
作者
Ryu, Joonjae [1 ,2 ]
Maravelias, Christos T. [3 ,4 ,5 ]
机构
[1] Univ Wisconsin, Dept Chem & Biol Engn, 1415 Engn Dr, Madison, WI 53706 USA
[2] Univ Wisconsin, DOE Great Lakes Bioenergy Res Ctr, 1552 Univ Ave, Madison, WI 53726 USA
[3] Princeton Univ, Dept Chem & Biol Engn, 50-70 Olden St, Princeton, NJ 08540 USA
[4] Princeton Univ, Andlinger Ctr Energy & Environm, 86 Olden St, Princeton, NJ 08540 USA
[5] DOE Great Lakes Bioenergy Res Ctr, Washington, DC 20585 USA
关键词
Distillation network; Process synthesis; Global optimization; Superstructure; MULTICOMPONENT DISTILLATION; GLOBAL OPTIMIZATION; INDUSTRIAL DISTILLATION; MINIMIZATION; FORMULATION; SEQUENCES; FRAMEWORK; DESIGN; FEED;
D O I
10.1016/j.ces.2021.116766
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
We propose a generalized superstructure-based distillation network synthesis model with improved modeling capabilities resulting in an extended solution space. The model can assign multiple mixtures to be separated (e.g., reactor network effluents) to different columns of the network while considering the interactions among different separation steps. In terms of outlets, products with general specifications, including pure components and multi-component mixtures, as well as streams without strict specifications (e.g., reactor recycle streams) can be readily handled. Furthermore, stream bypass is considered to avoid unnecessary separations, and thermal coupling is considered to yield novel solutions. The proposed model enables seamless integration with reactor network synthesis models thereby leading to solutions that are superior to the ones obtained by conventional sequential approaches. (c) 2021 Elsevier Ltd. All rights reserved.
引用
收藏
页数:18
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