A novel approach for infeasible path optimization of distillation-based flowsheets

被引:0
|
作者
Seidel T. [1 ]
Hoffmann A. [1 ]
Bortz M. [1 ]
Scherrer A. [1 ]
Burger J. [2 ]
Asprion N. [3 ]
Küfer K.-H. [1 ]
Hasse H. [4 ]
机构
[1] Fraunhofer Institute for Industrial Mathematics (ITWM), Fraunhofer-Platz 1, Kaiserslautern
[2] Chair of Chemical Process Engineering, Technical University of Munich, Campus Straubing for Biotechnology and Sustainability, Schulgasse 16, Straubing
[3] Chemical and Process Engineering BASF SE, Carl-Bosch-Str. 38, Ludwigshafen
[4] Laboratory of Engineering Thermodynamics (LTD), University of Kaiserslautern, Erwin-Schrödinger-Str. 44, Kaiserslautern
来源
关键词
Distillation; Optimization; Process simulation;
D O I
10.1016/j.cesx.2020.100063
中图分类号
学科分类号
摘要
In this work, a new approach for simultaneous steady state simulation and optimization of distillation-based flowsheets is presented. The process simulation is embedded in an optimization problem with a small number of optimization variables and constraints. Hence, no specialized solvers are needed. Moreover, an arbitrary number of specifications in the form of equalities or inequalities can be set in the problem formulation. This matches the process engineering demands usually much better than specifying a given quantity of fixed numbers. The remaining process variables for distillation columns are calculated from stage-to-stage using fixed-point iterations as developed and analyzed in previous work of the authors (Hoffmann et al., 2017). To illustrate the new approach, typical examples for process simulation and optimization of distillation-based flowsheets including several columns and also recycle streams are presented. For such distillation-based flowsheets an algorithm is presented that determines a possible calculation sequence of units within one iteration of the optimization algorithm. © 2020 The Authors
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