Binary interaction parameters of CO2−heavy-n-alkanes systems by using Peng–Robinson equation of state with modified alpha function-Reference-Cited by-同舟云学术

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Binary interaction parameters of CO2−heavy-n-alkanes systems by using Peng–Robinson equation of state with modified alpha function

Published:2016-06 Issue: Volume:417 Page:77-86
ISSN:0378-3812
Container-title:Fluid Phase Equilibria
language:en
Short-container-title:Fluid Phase Equilibria

Author:

Li Xiaoli,Yang Daoyong,Zhang Xuechao,Zhang Guangqing,Gao Junmin

Funder

Natural Sciences and Engineering Research Council (NSERC) of Canada

EHR Enhanced Hydrocarbon Recovery Inc.

University of Kansas

Publisher

Elsevier BV

Subject

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

Reference49 articles.

1. A generalized correlation for the interaction coefficients of CO2-hydrocarbon binary mixtures;Kordas;Fluid Phase Equilib.,1994

2. Equation of state modeling of the phase equilibria of asymmetric CO2 + n-alkane binary systems using mixing rules cubic with respect to mole fraction;Cismondi;J. Supercrit. Fluid,2010

3. Generalized interaction parameters for the Peng-Robinson equation of state: carbon dioxide-n-paraffin binary systems;Kato;Fluid Phase Equilib.,1981

4. Binary interaction parameters for nonpolar systems with cubic equations of state: a theoretical approach 1. CO2/hydrocarbons using SRK equation of state;Coutinho;Fluid Phase Equilib.,1994

5. Enhanced swelling effect and viscosity reduction of solvent(s)/CO2/heavy-oil systems;Li;SPE J.,2013

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