Research Article
Year 1988,
Volume: 34 Issue: 01.02, 94 - 102, 01.01.1899
Abstract
The Redlich-Kwong equation of State was used to calculate liquid and vapour phase fuga- cities of Acetic acid (l)-n. Heptane (2) and Acetic acid (l)-Benzene (2) Systems for predicting isothermal vapour-Iiquid equilibria. The binary interaction coefficients were obtained by a mi- nimization technique with the help of a Computer. The agreement, between the predicted and experimental equilibrium data allows the calculation of isothermal vapour-liquid data for Sys¬tems containing both polar and non-polar compounds.
References
- Communications Faculty of Sciences University of Ankara Series B Chemistry and Chemical Engineering
Year 1988,
Volume: 34 Issue: 01.02, 94 - 102, 01.01.1899
Abstract
References
- Communications Faculty of Sciences University of Ankara Series B Chemistry and Chemical Engineering
There are 1 citations in total.
Details
| Primary Language | English |
|---|---|
| Subjects | Chemical Engineering |
| Journal Section | Research Article |
| Authors | |
| Publication Date | January 1, 1899 |
| DOI | https://doi.org/10.1501/Commub_0000000491 |
| IZ | https://izlik.org/JA98TD65ZA |
| Published in Issue | Year 1988 Volume: 34 Issue: 01.02 |
Communications Faculty of Sciences University of Ankara Series B Chemistry and Chemical Engineering
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