An optimization strategy for nonlinear simulated moving bed chromatography: Multi-level optimization procedure MLOP)

被引:19
作者
Lim, YI [1 ]
机构
[1] Hankyong Natl Univ, Dept Chem Engn, Anseong 456749, Kyonggi Do, South Korea
关键词
simulated moving bed (SMB) chromatography; simulation and optimization; multi-level optimization procedure (MLOP); nonlinear adsorption isotherms; productivity; desorbent consumption;
D O I
10.1007/BF02705529
中图分类号
O6 [化学];
学科分类号
0703 [化学];
摘要
This paper presents a multi-level optimization strategy to obtain optimum operating conditions (four flow-rates and cycle time) of nonlinear simulated moving bed chromatography. The multi-level optimization procedure (MLOP) approaches systematically from initialization to optimization with two objective functions (productivity and desorbent consumption), employing the standing wave analysis, the true moving bed (TMB) model and the simulated moving bed (SMB) model. The procedure is constructed on a non-worse solution property advancing level by level and its solution does not mean a global optimum. That is, the lower desorbent consumption under the higher productivity is successively obtained on the basis of the SMB model, as the two SMB-model optimizations are repeated by using a standard SQP (successive quadratic programming) algorithm. This approach takes advantage of the TMB model as well as surmounts shortcomings of the TMB model in the general case of any nonlinear adsorption isotherm using the SMB model. The MLOP is evaluated on two nonlinear SMB cases characterized by i) quasi-linear/non-equilibrium and ii) nonlinear/nonequilibrium model. For the two cases, the MLOP yields a satisfactory solution for high productivity and low desorbent consumption within required purities.
引用
收藏
页码:836 / 852
页数:17
相关论文
共 24 条
[1]
Optimization of simulated moving bed plants with low efficient stationary phases: separation of fructose and glucose [J].
Beste, YA ;
Lisso, M ;
Wozny, G ;
Arlt, W .
JOURNAL OF CHROMATOGRAPHY A, 2000, 868 (02) :169-188
[2]
Design and optimisation of a simulated moving bed unit: role of deviations from equilibrium theory [J].
Biressi, G ;
Ludemann-Hombourger, O ;
Mazzotti, M ;
Nicoud, RM ;
Morbidelli, M .
JOURNAL OF CHROMATOGRAPHY A, 2000, 876 (1-2) :3-15
[3]
CHANG SC, 2002, AIAA20023890
[4]
Simulated moving-bed chromatography and its application to chirotechnology [J].
Juza, M ;
Mazzotti, M ;
Morbidelli, M .
TRENDS IN BIOTECHNOLOGY, 2000, 18 (03) :108-118
[5]
The application of simulated moving bed chromatography for the separation between 2,6-and 2,7-dimethylnaphthalene [J].
Kim, YD ;
Lee, JK ;
Cho, YS .
KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2001, 18 (06) :971-976
[6]
KLATT KU, 2002, AICHE S SERIES, V326, P239
[7]
Continuous separation of glucose and fructose at high concentration using two-section simulated moving bed process [J].
Lee, KN .
KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2003, 20 (03) :532-537
[8]
Multiobjective optimization in terms of economics and potential environment impact for process design and analysis in a chemical process simulator [J].
Lim, YI ;
Floquet, P ;
Joulia, X ;
Kim, SD .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (12) :4729-4741
[9]
LIM YI, 2004, IN PRESS CHEM ENG SC
[10]
LIM YI, 2004, IN PRESS COMPUT CHEM