| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 621647 | Chemical Engineering Research and Design | 2013 | 17 Pages |
Abstract
⺠Mathematical model for Co2+ ion extraction using HFSLM operated in recycling mode. ⺠Di-(2-ethylhexyl) phosphoric acid (D2EHPA) was used as an extractant. ⺠Counter-ion (H+) transport resistance has been incorporated in the model. ⺠Mass balance for D2EHPA has also been considered in the model. ⺠Metal-complex diffusivity (Dm) through the membrane phase was the only adjustable parameter.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Filtration and Separation
Authors
Prasad V. Vernekar, Yogesh D. Jagdale, Ashwin W. Patwardhan, Anand V. Patwardhan, Seraj A. Ansari, Prasanta K. Mohapatra, Vijay K. Manchanda,