Abstract
Numerical and analytical approaches are used to develop a mathematical model for the ion exchange in a column with a fluidized ion exchanger bed sectioned by perforated plates. The model is tested for adequacy using the ion exchange adsorption of copper ions on a Lewatit S100 cation exchanger (Germany) and nickel ions on a KU-2-8 cation exchanger in countercurrent perforated-plate columns.
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