Optimal synthesis of complex distillation columns using rigorous models

被引:74
作者
Grossmann, IE [1 ]
Aguirre, PA
Barttfeld, M
机构
[1] Carnegie Mellon Univ, Dept Chem Engn, Pittsburgh, PA 15213 USA
[2] INGAR Inst Desarrollo & Diseno, RA-3000 Santa Fe, Argentina
关键词
disjunctive programming; complex distillation columns; initialization;
D O I
10.1016/j.compchemeng.2005.02.030
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
The synthesis of complex distillation columns has remained a major challenge since the pioneering work by [Sargent, R.W.H., & Gamini-bandara, K. (1976). Optimal design of plate distillation columns. In L.C.W. Dixon (Ed.), Optimization in action. New York: Academic Press]. In this paper, we first provide a review of recent work for the optimal design of distillation of individual columns using tray-by-tray models. We examine the impact of different representations and models, NLP, mixed-integer nonlinear programming (MINLP) and generalized disjunctive programming (GDP), as well as the importance of appropriate initialization schemes. We next provide a review of the synthesis of complex column configurations for zeotropic mixtures and discuss different superstructure representations as well as decomposition schemes for tackling these problems. Finally, we briefly discuss extensions for handling azeotropic mixtures. Numerical examples are presented to demonstrate that effective computational strategies are emerging that are based on disjunctive programming models that are coupled with thermodynamic initialization models and integrated through hierarchical decomposition techniques. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1203 / 1215
页数:13
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