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Calculation of HmE for binary mixtures: some consequences of the conversion of cubic equations of state to hard-sphere versions
It has been reported by Mosedale and Wormald [1], and by Christensen et al. [2,3], that replacement in cubic equations of state (EOS) of the free volume term, 1/( V m- b), with a hard-sphere expression improves the fit to the enthalpies of mixing, H m E, at near critical, constant, temperatures and...
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Published in: | Thermochimica acta 1989-11, Vol.154 (1), p.107-117 |
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Main Author: | |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | It has been reported by Mosedale and Wormald [1], and by Christensen et al. [2,3], that replacement in cubic equations of state (EOS) of the free volume term, 1/(
V
m-
b), with a hard-sphere expression improves the fit to the enthalpies of mixing,
H
m
E, at near critical, constant, temperatures and pressures for binary mixtures. Further improvements can be obtained in some cases with Kreglewski's square-well combining rule for
a
12 [4], and with a temperature-dependent
b parameter [5]. For mixtures of CO
2 with a hydrocarbon, the improvements appear to allow estimates of
H
m
E data that are as reliable as correlations with one adjustable interaction parameter. Attempts to use a hard-sphere expression in the Peng-Robinson equation lead to an unacceptable EOS. Singularities can be used to forecast when a hard-sphere version will be unacceptable. |
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ISSN: | 0040-6031 1872-762X |
DOI: | 10.1016/0040-6031(89)87123-0 |