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

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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

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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