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The prediction of vapor—liquid equilibrium from heat of mixing data for binary hydrocarbon—ketone mixtures

✍ Scribed by C. Pando; J.A.R. Renuncio; R.W. Hanks; J.J. Christensen

Publisher
Elsevier Science
Year
1983
Tongue
English
Weight
994 KB
Volume
63
Category
Article
ISSN
0040-6031

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Ah&w&The parameters of the NRTL method are fitted, for binary hydrocarbon systems, on the activity coefficients calculated by the Flory-Hildebrand method with binary coefficients ii, of deviation from the geometric mean assumption for cohesive energy densities (NRTL-FH parameters). For aromatic satu