High-pressure vapour-liquid equilibria in binary mixtures of carbon dioxide and benzene compounds: experimental data for mixtures with ethylbenzene, isopropylbenzene, 1,2,4-trimethylbenzene, 1,3,5-trimethylbenzene, ethenylbenzene and isopropenylbenzene, and their correlation with the generalized Bender and Skjold-Jørgensen's group contribution equation of state-Reference-Cited by-同舟云学术

High-pressure vapour-liquid equilibria in binary mixtures of carbon dioxide and benzene compounds: experimental data for mixtures with ethylbenzene, isopropylbenzene, 1,2,4-trimethylbenzene, 1,3,5-trimethylbenzene, ethenylbenzene and isopropenylbenzene, and their correlation with the generalized Bender and Skjold-Jørgensen's group contribution equation of state

Published:1994-06 Issue: Volume:97 Page:167-189
ISSN:0378-3812
Container-title:Fluid Phase Equilibria
language:en
Short-container-title:Fluid Phase Equilibria

Author:

Bamberger Andreas,Schmelzer Jürgen,Walther Dieter,Maurer Gerd

Publisher

Elsevier BV

Subject

Physical and Theoretical Chemistry,General Physics and Astronomy,General Chemical Engineering

Reference41 articles.

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3. Modeling the vapor-liquid equilibria of 1,1,1-trichloroethane + carbon dioxide and toluene + carbon dioxide at 308, 323, and 353 K;Fink;Ind. Eng. Chem. Res.,1990

4. Solubilities of carbon dioxide in heavy normal paraffins (C20-C44) at pressures to 9.6 MPa and temperatures from 323 to 423 K;Gasem;J. Chem. Eng. Data,1985

5. Phase Equilibrium for carbon dioxide-benzene at 313.2, 353.2, and 393.2 K;Gupta;J. Chem. Eng. Data,1982

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