Comparison of Mass Transfer Coefficient Approach and Nernst–Planck Formulation in the Reactive Transport Modeling of Co, Ni, and Ag Removal by Mixed-Bed Ion-Exchange Resins

Author:

Bachet Martin12,Jauberty Loïc2,De Windt Laurent2,Tevissen Etienne3,de Dieuleveult Caroline2,Schneider Hélène1

Affiliation:

1. Département Matériaux et Mécanique des Composants, EDF R&D, Avenue des Renardières - Ecuelles, 77818 Moret sur Loing cedex, France

2. Centre de Géosciences, Mines-ParisTech, 77305 Fontainebleau cedex, France

3. DEN/CAD/STCP/LHC, CEA, 13108 Saint-Paul lez Durance cedex, France

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Reference18 articles.

1. Rate of Ion Exchange

2. Binary Liquid-Phase Mass Transport in Mixed-Bed Ion Exchange at Low Solute Concentration

3. True multi-component mixed-bed ion-exchange modeling

4. Roth, D. W. H.Ternary Ion Exchange in Fixed Beds: Equilibrium and Dynamics. Ph.D. Dissertation,New Jersey Institute of Technology:Newark, NJ, 1985.

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