A Pseudo-Transient Optimization Framework for Periodic Processes: Pressure Swing Adsorption and Simulated Moving Bed Chromatography

被引:26
作者
Tsay, Calvin [1 ]
Pattison, Richard C. [1 ]
Baldea, Michael [1 ]
机构
[1] Univ Texas Austin, McKetta Dept Chem Engn, Austin, TX 78712 USA
基金
美国国家科学基金会;
关键词
pressure-swing adsorption; chromatography; periodic processes; dynamic optimization; pseudo-transient simulation; POSTCOMBUSTION CO2 CAPTURE; DYNAMIC OPTIMIZATION; PROCESS FLOWSHEETS; SEPARATION; UNCERTAINTY; STRATEGIES; OPERATION; MODELS; CYCLES;
D O I
10.1002/aic.15987
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Periodic systems are widely used in separation processes and in reaction engineering. They are designed for and operated at a cyclic steady state (CSS). Identifying and optimizing the CSS has proven to be computationally challenging. A novel framework for equation-oriented simulation and optimization of cyclic processes is introduced. A two-step reformulation of the process model is proposed, comprising, (1) a full discretization of the time and spatial domains and (2) recasting the discretized model as a differential-algebraic equation system, for which theoretical stability guarantees are provided. Additionally, a mathematical, structural connection between the CSS constraints and material recycling is established, which allows us to deal with these conditions via a "tearing" procedure. These developments are integrated in a pseudo-transient design optimization framework and two extensive case studies are presented: a simulated moving bed chromatography system and a pressure swing adsorption process. (C) 2017 American Institute of Chemical Engineers
引用
收藏
页码:2982 / 2996
页数:15
相关论文
共 31 条