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 |
|---|---|
| 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 |
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