Calculations of Vapor-liquid Equilibria of Hydrogen-Containing Systems with Peng-Robinson Equation of State-Modification of Parameters for the Supercritical Gas
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Calculations of Vapor-liquid Equilibria of Hydrogen-Containing Systems with Peng-Robinson Equation of State-Modification of Parameters for the Supercritical Gas
CIESC JournalIssue 1, (1989)
作者机构:
北京化工学院,北京化工学院 ,北京,北京
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Online First:25 February 1989,
Published:25 February 1989
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Liu Kunyuan and Wang Wenchuan(Beijing Institute of Chemical Technology, Beijing). Calculations of Vapor-liquid Equilibria of Hydrogen-Containing Systems with Peng-Robinson Equation of State-Modification of Parameters for the Supercritical Gas[J]. CIESC Journal, 1989, (1).
DOI:
Liu Kunyuan and Wang Wenchuan(Beijing Institute of Chemical Technology, Beijing). Calculations of Vapor-liquid Equilibria of Hydrogen-Containing Systems with Peng-Robinson Equation of State-Modification of Parameters for the Supercritical Gas[J]. CIESC Journal, 1989, (1).DOI:
Calculations of Vapor-liquid Equilibria of Hydrogen-Containing Systems with Peng-Robinson Equation of State-Modification of Parameters for the Supercritical Gas
Peng-Robinson equation of state was modified to represent vapor-liquid equilibria tor hydrogen-hydrocarbon binary systems. A new expression of the temperature dependent parameter for the supercritical gas hydrogen
and binary interaction parameters were introduced to improve description of vapor-liquid equilibria for 19 binary systems. Results show that this work is superior to previous researches
and to Mathias RKS and CCOR equation of state for heavy hydrocarbons
C6 to C16
in particular. Moreover
estimations of p-V-T relation and second virial coefficients of hydrogen from our modification are in good agreement with the experimental data.