Improved Modeling of the Phase Behavior of Asymmetric Hydrocarbon Mixtures with the Peng−Robinson Equation of State Using a Different Temperature Dependency of the Parameter a-Reference-Cited by-同舟云学术

Improved Modeling of the Phase Behavior of Asymmetric Hydrocarbon Mixtures with the Peng−Robinson Equation of State Using a Different Temperature Dependency of the Parameter a

Published:1998-03-18 Issue:5 Volume:37 Page:1651-1662
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Flöter E.¹,de Loos Th. W.¹,de Swaan Arons J.¹

Affiliation:

1. Laboratory of Applied Thermodynamics and Phase Equilibria, Delft University of Technology, Julianalaan 136, 2628 BL Delft, The Netherlands

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/ie970644o

Reference39 articles.

1. Vapor-Liquid Critical Properties of Elements and Compounds. 2. Normal Alkanes

2. Vapor-Liquid Critical Properties of Elements and Compounds. 3. Aromatic Hydrocarbons

3. Prediction/correlation of vapor-liquid equilibria in synthetic gas and oil systems

4. Excess volumes and saturation pressures for the system methane + n-tetracosane at 374 K. Representation by improved EOS mixing rules

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