Comparison of modified alpha functions of the PR-EoS for volume and enthalpy prediction of natural gases

Author:

GONÇALVES ANDRÉ F.1ORCID,COSTA ANDRÉA O.S. DA1ORCID,COSTA JUNIOR ESLY F. DA1ORCID

Affiliation:

1. Universidade Federal de Minas Gerais, Brazil

Publisher

FapUNIFESP (SciELO)

Subject

Multidisciplinary

Reference29 articles.

1. Generalized binary interaction parameters for the Peng–Robinson equation of state;ABUDOUR AM;Fluid Phase Equilibr,2014

2. Measurements of enthalpy and phase equilibrium for simulated natural gas mixtures and correlation of the results by a modified Starling equation;ASHTON GJ;Cryogenics,1980

3. Development of a new alpha function for the Peng-Robinson equation of state: Comparative study of alpha function models for pure gases (natural gas components) and water-gas systems;COQUELET C;Int J Thermphys,2004

4. Improving predictions of equation of state by modifying its parameters for super critical components of hydrocarbon reservoir fluids;DANESH A;Fluid Phase Equilibr,1995

5. 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;FLÖTER E;Ind Eng Chem Res,1998

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