Application of the Maxwell–Stefan approach to ion exchange in microporous materials. Batch process modelling

2007 ◽  
Vol 62 (23) ◽  
pp. 6939-6946 ◽  
Author(s):  
Carlos M. Silva ◽  
Patrícia F. Lito
2020 ◽  
Vol 93 (4) ◽  
pp. 595-602
Author(s):  
N. V. Chukanov ◽  
N. A. Chervonnaya ◽  
O. N. Kazheva ◽  
V. N. Ermolaeva ◽  
D. A. Varlamov ◽  
...  

2008 ◽  
Vol 273-276 ◽  
pp. 776-781 ◽  
Author(s):  
Patricia F. Lito ◽  
Carlos Manuel Silva

Two models comprising external and intraparticle mass transfer resistances developed to describe ion exchange in microporous materials are compared. Maxwell-Stefan and Nernst-Planck equations account for both concentration and electric potential gradients. However, under certain conditions, Maxwell-Stefan approach can be more advantageous particularly due to taking into account ion-ion and ion-solid interactions separately. The models were tested and compared with data available in the literature, namely batch experiments on cadmium (II) removal from aqueous solution using ETS-4 microporous titanosilicate. Calculated results reveal both models provide good and similar representations as well as fine predictive capability. Therefore, under the conditions investigated, both models can be successfully applied to describe intraparticle ionic transport.


2007 ◽  
Vol 17 (5-6) ◽  
pp. 471-479 ◽  
Author(s):  
Xiaoling Ou ◽  
Elaine Martin

2004 ◽  
Vol 37 (9) ◽  
pp. 817-822
Author(s):  
Xiaoling Ou ◽  
Julian Morris ◽  
Elaine Martin

2021 ◽  
Author(s):  
Daniel N. Rainer ◽  
Russell Morris

Zeolites are a class of microporous materials with tremendous value for large scale industrial applications such as catalysis, ion exchange, or gas separation. In addition to naturally ocurring variants, zeolites...


2012 ◽  
Vol 66 (12) ◽  
Author(s):  
Jiří Kaláb ◽  
Zdeněk Palatý

AbstractBatch electrodialysis of aqueous solutions of oxalic acid was investigated using a laboratory electrodialyzer ED-Z mini equipped with ion-exchange membranes Ralex-AMH-PES and Ralex-CMHPES (Mega, Stráž pod Ralskem, Czech Republic). The paper presents a mathematical model which enables to predict changes in the oxalic acid concentrations in the diluate and concentrate compartments during the electrodialysis process under various conditions specified by combinations of the initial acid concentrations with current densities. The calculation proved a good agreement between the developed model and the experimental results.


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