Abstract
A comparison between the Stefan-Maxwell and the Fickian mass transfer-based mathematical models for predicting the air-gap membrane distillation process performance in breaking azeotropic mixtures such as formic acid/ water system is carried out in this paper. The predictions of Stefan-Maxwell model which incorporated temperature and concentration polarization effects were closer to the reported literature experimental data than the Fickian-based model that was developed by Udriot et al. The model was also used to predict the process behavior under other experimentally unstudied process parameters.
Original language | British English |
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Pages (from-to) | 879-888 |
Number of pages | 10 |
Journal | International Communications in Heat and Mass Transfer |
Volume | 26 |
Issue number | 6 |
DOIs | |
State | Published - Aug 1999 |