Abstract
The use of the results of a series of field tests in the modeling of a packed liquid—liquid extraction column is demonstrated. In the models developed the kerosene—sulfur dioxide system may be represented either by a pseudo ternary or a multicomponent mixture. The parameters determined from the field tests consisted of the number of mass transfer sections or plates and component efficiency factors. Also, a rapid and stable calculational procedure, based on the θ-method of convergence, for solving liquid—liquid extraction problems is presented.
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