Abstract
The partial condensation or dephlegmation process is generally used for the production of liquid reflux and vaporous disdilate with an additional fractionation in wetted wall column heat exchangers. All known calculations of the performance of vapour condensers are based on a film model, originally derived for binary vapour systems by Ackermann and by Colburn and Drew and generalized for multi-component vapour systems by Standart and Krishna using a general matrix models for the multi-component mass transfer with the more accurate model of Standart and Krishna is given for the partial condensation of a ternary vapour system.
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