Generalized optimization-based synthesis of membrane systems for multicomponent gas mixture separation

被引:18
作者
Taifan, Garry S. P. [1 ,2 ]
Maravelias, Christos T. [1 ,2 ,3 ]
机构
[1] Princeton Univ, Dept Chem & Biol Engn, 50-70 Olden St, Princeton, NJ 08540 USA
[2] DOE Great Lakes Bioenergy Res Ctr, Madison, WI USA
[3] Princeton Univ, Andlinger Ctr Energy & Environm, 86 Olden St, Princeton, NJ 08540 USA
关键词
Global optimization; Membrane gas separation; Process synthesis; CO2; CAPTURE; HIGH-FLUX; PERMEATION; MODEL; DESIGN; REPLACEMENT;
D O I
10.1016/j.ces.2022.117482
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Synthesizing a membrane system to separate multicomponent gas mixture is challenging due to the combinatorial number of feasible configurations and the difficulties in describing the multicomponent permeators. We present a mixed-integer nonlinear programming (MINLP) model for synthesizing membrane systems for multicomponent gas mixture separation. The approach employs a richly connected superstructure to represent numerous potential system configurations, and different physics-based surrogate permeator models, such as countercurrent flow or crossflow, to be used in each stage. Moreover, to describe realistic systems, pressure drop equations can be included. We also present solution methods to accelerate the solution process. Through a case study of natural gas sweetening, we demonstrate that the proposed approach is able to obtain good solutions using an off-the-shelf global optimization solver. Finally, we expand the conventional membrane system synthesis problem by introducing feed variability in our model through a case study of an integrated reactor-separation system. (C) 2022 Elsevier Ltd. All rights reserved.
引用
收藏
页数:14
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