Isoplethic Method to Estimate Critical Lines for Binary Fluid Mixtures from Subcritical Vapor−Liquid Equilibrium: Application to the Azeotropic Mixtures R32 + C3H8 and R125 + C3H8-Reference-Cited by-同舟云学术

Isoplethic Method to Estimate Critical Lines for Binary Fluid Mixtures from Subcritical Vapor−Liquid Equilibrium: Application to the Azeotropic Mixtures R32 + C3H8 and R125 + C3H8

Published:2001-09-15 Issue:21 Volume:40 Page:4610-4614
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Van Poolen Lambert J.¹,Holcomb Cynthia D.¹,Rainwater James C.¹

Affiliation:

1. Physical and Chemical Properties Division, Chemical Science and Technology Laboratory, National Institute of Standards and Technology, 325 Broadway, Boulder, Colorado 80305-3328

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/ie010215x

Reference13 articles.

1. Extended phase rule for non-reactive, multiphase, multicomponent chemical systems

2. Experimental method for obtaining critical densities of binary mixtures: application to ethane + n-butane

3. Vapor-liquid equilibria of ternary mixtures in the critical region on paths of constant temperature and overall composition

4. A study of the volumetric and phase behavior of binary systems. Part I. Critical properties of propane-perfluorocyclobutane mixtures

5. A study of the volumetric and phase behavior of binary systems. Part II. Vapor-liquid equilibria and azeotropic states of propane-perfluorocyclobutane mixtures

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