Please use this identifier to cite or link to this item:
|Title:||Development of a Solvent Extraction Model for Process Tests in Short Residence Time Centrifugal Contactors|
|Authors:||MAGNUSSON Daniel; MALMBECK Rikard|
|Citation:||SOLVENT EXTRACTION AND ION EXCHANGE vol. 30 no. 2 p. 115-126|
|Publisher:||TAYLOR & FRANCIS INC|
|Type:||Articles in periodicals and books|
|Abstract:||A computer program has been developed for optimization and modelling of counter–current solvent extraction processes. The distribution between the phases is calculated by either D-ratio functions or by a novel kinetic model for the transfer between the phases. The kinetic model is important to use when slow extraction kinetics yields D-ratios far from equilibrium. Transfer rate data was investigated in a single stage centrifugal contactor, modified for internal recirculation of the phases. Using this methodology a demonstration process for the recovery of minor actinides in a counter–current centrifugal contactor system using CyMe4-BTBP was modelled with excellent agreement towards the experimental values.|
|JRC Directorate:||Nuclear Safety and Security|
Files in This Item:
There are no files associated with this item.
Items in repository are protected by copyright, with all rights reserved, unless otherwise indicated.