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Cited article:

Mathematical modeling and optimization of industrial scale ELUXYL simulated moving bed (SMB)

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Separation and Purification Technology 248 116961 (2020)
https://doi.org/10.1016/j.seppur.2020.116961

Modelling of a Simulated Moving Bed in case of non-ideal hydrodynamics

L. Fangueiro Gomes, F. Augier, D. Leinekugel-le-Cocq, I. Vinkovic and S. Simoëns
Chemical Engineering Science 153 188 (2016)
https://doi.org/10.1016/j.ces.2016.07.027

Single- and Multicomponent Vapor-Phase Adsorption of Xylene Isomers and Ethylbenzene in a Microporous Metal−Organic Framework

Marco P. M. Nicolau, Patrick S. Bárcia, Jose M. Gallegos, et al.
The Journal of Physical Chemistry C 113 (30) 13173 (2009)
https://doi.org/10.1021/jp9006747

Adaptive Soft-sensor Modeling Algorithm Based on FCMISVM and Its Application in PX Adsorption Separation Process

Yongfeng FU, Hongye SU, Ying ZHANG and Jian CHU
Chinese Journal of Chemical Engineering 16 (5) 746 (2008)
https://doi.org/10.1016/S1004-9541(08)60150-0

Efficient optimization of simulated moving bed processes

A. Toumi, S. Engell, M. Diehl, H.G. Bock and J. Schlöder
Chemical Engineering and Processing: Process Intensification 46 (11) 1067 (2007)
https://doi.org/10.1016/j.cep.2006.06.026

Understanding and revamping of industrial scale SMB units for p‐xylene separation

Mirjana Minceva and Alírio E. Rodrigues
AIChE Journal 53 (1) 138 (2007)
https://doi.org/10.1002/aic.11062

Influence of the Transfer Line Dead Volume on the Performance of an Industrial Scale Simulated Moving Bed for p-Xylene Separation

Mirjana Minceva and Alirio E. Rodrigues
Separation Science and Technology 38 (7) 1463 (2003)
https://doi.org/10.1081/SS-120019088