Methanehydrocarbon interaction parameters correlation for the Peng-Robinson and the t-mPR equation of state

 
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1995 (EN)

Methanehydrocarbon interaction parameters correlation for the Peng-Robinson and the t-mPR equation of state (EN)

Kordas, A (EN)
Tassios, D (EN)
Magoulas, K (EN)
Stamataki, S (EN)

Generalized expressions for the interaction coefficients (kij) of CH4 hydrocarbon binary systems are presented for a modified and translated Peng-Robinson equation of state (t-mPR). The correlations involve the acentric factor of the heavier hydrocarbon and cover the CH4 n-alkane systems up to n-C44 plus isomers and cycloalkanes. Typical errors in bubble point pressure predictions are below 5%, similar to those obtained by fitting the T-P-x data. Successful predictions of saturated liquid and vapor volumes are also obtained. For the CH4 non-alkane systems average kij values are recommended, since the lack of data for an adequate number of systems does not allow the development of a generalized correlation. The proposed correlations can be used with the Peng-Robinson equation of state as well. © 1995. (EN)

journalArticle (EN)

Methane (EN)
Methods of calculation (EN)
Interaction parameters (EN)
Theory (EN)
Empirical (EN)
Hydrocarbons (EN)
Equations of state of liquids (EN)
Molecular size (EN)
Correlation methods (EN)
Binary mixtures (EN)
Chemistry, Physical (EN)
Pressure (EN)
Isomers (EN)
Thermodynamics (EN)
Liquid methane (EN)
Bubble point pressure (EN)
Engineering, Chemical (EN)
Cycloalkanes (EN)
Calculations (EN)
Phase equilibria (EN)
Thermodynamic properties (EN)
Phase behavior (EN)


Fluid Phase Equilibria (EN)

English

1995 (EN)

33 (EN)
44 (EN)
1 (EN)
112 (EN)
0378-3812 (EN)
10.1016/0378-3812(95)02787-F (EN)
ISI:A1995TE24200003 (EN)

ELSEVIER SCIENCE BV (EN)




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