| 1 |
Effect of Dead Volumes on the Performance of an Industrial-Scale Simulated Moving-Bed Parex Unit for p-Xylene Purification
Silva MSP, Rodrigues AE, Mota JPB
AIChE Journal, 62(1), 241, 2016 |
| 2 |
Modeling and Simulation of an Industrial-Scale Parex Process
Silva MSP, Rodrigues AE, Mota JPB
AIChE Journal, 61(4), 1345, 2015 |
| 3 |
Mathematical Modeling of a Simulated Moving-Bed Adsorption Process: Parex (TM) Technology as a Case Study
Rezazadeh M, Esfahani MS, Rahimi A, Ehsani MR
Chemical Engineering & Technology, 38(5), 759, 2015 |
| 4 |
Adsorption Equilibrium and Kinetics of the Parex' Feed and Desorbent Streams from Batch Experiments
Silva MSP, Mota JPB, Rodrigues AE
Chemical Engineering & Technology, 37(9), 1541, 2014 |
| 5 |
Adsorbent Evaluation Based on Experimental Breakthrough Curves: Separation of p-Xylene from C8 Isomers
Silva MSP, Moreira MA, Ferreira AFP, Santos JC, Silva VMTM, Gomes PS, Minceva M, Mota JPB, Rodrigues AE
Chemical Engineering & Technology, 35(10), 1777, 2012 |
| 6 |
Fixed-bed adsorption of aromatic C-8 isomers: Breakthrough experiments, modeling and simulation
Silva MSP, Mota JPB, Rodrigues AE
Separation and Purification Technology, 90, 246, 2012 |
| 7 |
Modeling and simulation of a simulated moving bed for adsorptive para-xylene separation
Lee J, Shin NC, Lim Y, Han C
Korean Journal of Chemical Engineering, 27(2), 609, 2010 |
| 8 |
Influence of the transfer line dead volume on the performance of an industrial scale simulated moving bed for p-xylene separation
Minceva M, Rodrigues AE
Separation Science and Technology, 38(7), 1463, 2003 |
