Simulation Study of a Multistage Mixer-Settler Extractor

A multistage mixer-settler extractor described in earlier hydrodynamic studies was simulated on a computer. A mass transfer mechanism was derived based on a pseudo distribution constant and a pseudo first-order rate constant. The constants were adjusted to give the proper output concentrations and proper form of the stage-wise concentrations. The results obtained by computer simulation of start-up conditions show very good agreement with experimental data. A second simulation was constructed which demonstrated that the model can be greatly simplified and still yield good results.