Multi-column chromatographic process development using simulated moving bed superstructure and simultaneous optimization - Model correction framework

被引:26
|
作者
Sreedhar, Balamurali [1 ]
Kawajiri, Yoshiaki [1 ]
机构
[1] Sch Chem & Biomol Engn, Atlanta, GA 30332 USA
关键词
Preparative; Chromatography; SMB; Superstructure; Optimization; SOMC; PREDICTION-CORRECTION METHOD; TROGERS BASE ENANTIOMERS; SEPARATION PROCESSES; SMB CHROMATOGRAPHY; OUTLET STREAMS; DEAD VOLUME; OPERATION; UNITS; IDENTIFICATION; ADSORPTION;
D O I
10.1016/j.ces.2014.05.004
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this work, we demonstrate an improved framework for simulated moving bed (SMB) chromatographic process development using a superstructure formulation. Various optimal column configurations and operations are obtained by solving a multi-objective optimization problem representing the superstructure by maximizing feed throughput and minimizing desorbent usage. In order to resolve the model mismatch with experimental data, here we utilize the simultaneous optimization - model correction (SOMC) method in which process optimization is carried out in tandem with model correction using data obtained from experimental evaluations. The potential of the superstructure-SOMC framework has been demonstrated by separating glucose and fructose using columns packed with a cation exchange resin with water as the mobile phase. The optimal operation modes found using the superstructure included standard SMB, three zone (3Z) operation, intermittent SMB (I-SMB) and a newly found outlet stream swing (OSS) - partial feed (PF) hybrid operation. All configurations were experimentally implemented using a Semba Octave (TM) 100 Chromatography System. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:428 / 441
页数:14
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