A Framework for the Systematic Design of Hybrid Separation Processes

›› 2008, Vol. 16 ›› Issue (3): 333-342.

• • 下一篇

A Framework for the Systematic Design of Hybrid Separation Processes

Wolfgang Marquardt, Sven Kossack, Korbinian Kraemer

Process Systems Engineering and Center for Computational Engineering Science, RWTH Aachen University, D-52064 Aachen, Germany

收稿日期:2007-09-20 修回日期:2008-03-19 出版日期:2008-06-28 发布日期:2008-06-28
通讯作者: Wolfgang Marquardt,E-mail:Wolfgang.Marquardt@avt.rwthaachen.de
基金资助:
the Deutsche Forschungsgemeinschaft (German Research Foundation);DAAD (German Academic Exchange Service) and FUNDAYACUCHO;and Bayer Technology Services

A Framework for the Systematic Design of Hybrid Separation Processes

Wolfgang Marquardt, Sven Kossack, Korbinian Kraemer

Process Systems Engineering and Center for Computational Engineering Science, RWTH Aachen University, D-52064 Aachen, Germany

Received:2007-09-20 Revised:2008-03-19 Online:2008-06-28 Published:2008-06-28
Supported by:
the Deutsche Forschungsgemeinschaft (German Research Foundation);DAAD (German Academic Exchange Service) and FUNDAYACUCHO;and Bayer Technology Services

摘要/Abstract

摘要： The design of optimal separation flow sheets for multi-component mixtures is still not a solved problem. This is especially the case when non-ideal or azeotropic mixtures or hybrid separation processes are considered. We review recent developments in this field and present a systematic framework for the design of separation flow sheets. This framework proposes a three-step approach. In the first step different flow sheets are generated. In the second step these alternative flow sheet structures are evaluated with shortcut methods. In the third step a rigorous mixed-integer nonlinear programming (MINLP) optimization of the entire flow sheet is executed to determine the best alternative. Since a number of alternative flow sheets have already been eliminated, only a few optimization runs are necessary in this final step. The whole framework thus allows the systematic generation and evaluation of separation processes and is illustrated with the case study of the separation of ethanol and water.

关键词: process synthesis, distillation design, rectification body method, mixed-integer nonlinear programming

Abstract: The design of optimal separation flow sheets for multi-component mixtures is still not a solved problem. This is especially the case when non-ideal or azeotropic mixtures or hybrid separation processes are considered. We review recent developments in this field and present a systematic framework for the design of separation flow sheets. This framework proposes a three-step approach. In the first step different flow sheets are generated. In the second step these alternative flow sheet structures are evaluated with shortcut methods. In the third step a rigorous mixed-integer nonlinear programming (MINLP) optimization of the entire flow sheet is executed to determine the best alternative. Since a number of alternative flow sheets have already been eliminated, only a few optimization runs are necessary in this final step. The whole framework thus allows the systematic generation and evaluation of separation processes and is illustrated with the case study of the separation of ethanol and water.

Key words: process synthesis, distillation design, rectification body method, mixed-integer nonlinear programming

Wolfgang Marquardt, Sven Kossack, Korbinian Kraemer. A Framework for the Systematic Design of Hybrid Separation Processes[J]. , 2008, 16(3): 333-342.

参考文献

1 Widagdo,S.,Seider,W.D.,"Azeotropic distillation",AIChE J.,42,96-130(1996).
2 Doherty,M.F.,Malone.M.F.,Conceptual Design of Distillation Systems,McGraw-Hill,New York(2001).
3 Douglas,J.M.,Conceptual Design of Chemical Processes,McGraw-Hill,New York(1988).
4 DeVilliers,W.E.,French,R.N.,Koplos,G.J.,"Navigate phase equilibria via residue curve maps",Chem.Eng.Prog.,98,66(2002).
5 Underwood,A.,"Fractional distillation of multi-component mixtures",Chem.Eng.Progress,44,603(1948).
6 Bausa,J.,von Watzdorf,R.,Marquardt,W.,"Shortcut methods for non-ideal multi-component distillation(1) Simple columns",AIChE J.,44,2181-2198(1998).
7 Levy,S.G.,van Dongen,D.B.,Doherty,M.F.,"Design and synthesis of homogeneous azeotropic distillations(2) Minimum reflux calculations for non-ideal and azeotropic columns",Ind.Eng.Chem.Fundam.,24,463-474(1985).
8 Liu,G.L.,Jobson,M.,Smith,R.,Wahnschafft,O.M.,"Shortcut design method for columns separating azeotropic mixtures",Ind.Eng.Chem.Res.,43,3908-3923(2004).
9 Julka,V.,Doherty,M.,"Geometric behavior and minimum flows for non-ideal multi-component distillation",Chem.Eng.Sci.,45,1801(1990).
10 Bauer,M.H.,Stichlmair,J.,"Design and economic optimization of azeotropic distillation processes using mixed-integer nonlinear programming",Comput.Chem.Eng.,22,1271-1286(1998).
11 Dunnebier,G.,Pantelides,C.C.,"Optimal design of thermally coupled distillation columns",Ind.Eng.Chem.Res.,38,162-176(1999).
12 Viswanathan,J.,Grossmann,I.E.,"Optimal feed locations and number of trays for distillation columns with multiple feeds",Ind.Eng.Chem.Res.,32,2942-2949(1993).
13 Kossack,S.,Kraemer,K.,Marquardt,W.,"Efficient optimization based design of distillation columns for homogenous azeotropic mixtures",Ind.Eng.Chem.Res.,45,8492-8502(2006).
14 Rooks,R.E.,Julka,V.,Doherty,M.F,Malone,M.F.,"Structure of distillation regions for multi-component azeotropic mixtures",AIChE J.,44,1382-1391(1998).
15 Harper,P.M.,Gani,R.,"A multi-step and multi-level approach for computer aided molecular design",Comp.Chem.Eng.,24,677-683(2000).
16 Kossack,S.,Kraemer,K.,Gani,R.,Marquardt,W.,"A systematic synthesis framework for extractive distillation processes",In:ECCE6 Book of Abstracts,Gani,R.,Dam-Johansen,K.,eds.,Copenhagen(2007).
17 Muller,D.,Marquardt,W.,"Experimental verification of multiple steady states in heterogeneous azeotropic distillation",Ind.Eng.Chem.Res.,36,5410-5418(1997).
18 Ryan,P.J.,Doherty,M.F.,"Design/optimization of ternary heterogeneous azeotropic distillation sequences",AIChE J.,35,1592-1601(1989).
19 Urdaneta,R.Y.,Bausa,J.,Bruggemann,S.,Marquardt,W.,"Analysis and conceptual design of ternary heterogeneous distillation processes",Ind.Eng.Chem.Res.,41,3849-3866(2002).
20 Bausa,J.,Marquardt,W.,"Shortcut design methods for hybrid membrane/distillation processes for the separation of non-ideal multi-component mixtures",Ind.Eng.Chem.Res.,39,1658-1672(2000).
21 Wallert,C.,"Conceptual design and economic analysis of heterogeneous separation processes with shortcut methods",PhD Thesis,RWTH Aachen,VDI Verlag,Dusseldorf(2008).
22 von Watzdorf,R.,Bausa,J.,Marquardt,W.,"Shortcut methods for non-ideal multi-component distillation(2) Complex columns",AIChE J.,45,1615-1628(1999).
23 Bruggemann,S.,Marquardt,W.,"Rapid screening of design alternatives for non-ideal multi-product distillation processes",Comput.Chem.Eng.,29,165-179(2005).
24 Bruggemann,S.,Marquardt,W.,"Shortcut methods for non-ideal multi-component distillation(3) Extractive distillation columns",AIChE J.,50,1129-1149(2004).
25 Pham,H.N.,Ryan,P.J.,Doherty,M.F.,"Design and minimum reflux for heterogeneous azeotropic distillation columns",AIChE J.,35,1585-1591(1989).
26 Pham,H.N.,Doherty,M.F.,"Design and synthesis of heterogeneous azeotropic distillations(Ⅲ) Column sequences",Chem.Eng.Sci.,45,1845(1990).
27 Wellinghoff,G,Wintermantel,K.,"Melt crystallization:theoretical premises and technical limitations",International Chemical Engineering,34(1),17-27(1994).
28 Bruggemann,S.,"Rapid screening of conceptual design alternatives for distillation processes",Ph D Thesis,RWTH Aachen,VDI Verlag,Dusseldorf(2005).
29 Kraemer,K.,Kossack,S.,Marquardt,W.,"An efficient solution method for the MINLP optimization of chemical processes",In:Proceedings of the 17th European Symposium on Computer Aided Process Engineering,Plesu,V.,Agachi,ES.,eds.,Bucharest(2007).
30 Kossack,S.,Kraemer,K.,Marquardt,W.,"Combining shortcut methods and rigorous MINLP optimization for the design of distillation processes for homogeneous azeotropic mixtures",In:Distillation & Absorption 2006,Sorensen,E.,ed.,IChemE,London,122-131(2006).
31 Knapp,J.P.,Doherty,M.F.,"A new pressure-swing-distillation process for separating homogeneous azeotropic mixtures",Ind.Eng.Chem.Res.,31,346-357(1992).
32 Stichlmair,J.G.,Fair J.R.,Distillation-Principles and Practices,Wiley-VCH,New York(1998).
33 Blass,E.,Chemical Process Design,Salle & Sauerlander,Frankfurt am Main(1989).

[1]	Danlei Chen, Xue Ma, Yiqing Luo, Yingjie Ma, Xigang Yuan. Synthesis of refrigeration system based on generalized disjunctive programming model[J]. Chinese Journal of Chemical Engineering, 2018, 26(8): 1613-1620.
[2]	Yiqing Luo, Liang Kong, Xigang Yuan. A systematic approach for synthesizing a low-temperature distillation system[J]. Chinese Journal of Chemical Engineering, 2015, 23(5): 789-795.
[3]	Arwa H. Rabie, Mahmoud M. El-Halwagi. Synthesis and Scheduling of Optimal Batch Water-recycle Networks[J]. , 2008, 16(3): 474-479.
[4]	石磊, 姚平经. 多目标进化算法求解过程综合中的混合整数线性规划(MILP)与混合整数非线性规划问题(MINLP)[J]. , 2001, 9(2): 173-178.
[5]	钱宇, KristianM.Lien. A FUZZY MATCH BASED EXPERT SYSTEM FOR SYNTHESIS OF SEPARATION PROCESSES[J]. , 1996, 4(2): 174-182.

A Framework for the Systematic Design of Hybrid Separation Processes

A Framework for the Systematic Design of Hybrid Separation Processes

PDF (PC)

可视化

摘要/Abstract

引用本文

使用本文

参考文献

相关文章 5

编辑推荐

Metrics

本文评价