Abstract
The UNIFAC model is extended to the prediction of vapor-liquid equilibria of polymer solutions using a proposed relation between the volume parameter r(n) for an n-mer polymer and that r(1) for the monomer. The modified UNIFAC model does not require a free-volume term as does the UNIFAC-FV model. As a result, no additional information is needed for the vapor-liquid equilibria Eq. (1a) calculation of polymer solutions other than the original UNIFAC group parameters. For 51 binary polymer-solvent systems, the total average absolute deviation of solvent activities in polymer solutions was 6.8% for the modified UNIFAC model versus 7.4% for the UNIFAC-FV model and 18.7% for the original UNIFAC model.
Original language | English |
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Pages (from-to) | 97-106 |
Number of pages | 10 |
Journal | Fluid Phase Equilibria |
Volume | 123 |
Issue number | 1-2 |
DOIs | |
Publication status | Published - 1996 Aug 15 |
Externally published | Yes |
Keywords
- Excess function
- Polymer solution
- UNIFAC model
- Vapor-liquid equilibria
ASJC Scopus subject areas
- Chemical Engineering(all)
- Physics and Astronomy(all)
- Physical and Theoretical Chemistry