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Vapor‐liquid equilibrium in the ethane‐carbon dioxide system
Author(s) -
Hamam Salah E. M.,
Lu Benjamin C. Y.
Publication year - 1974
Publication title -
the canadian journal of chemical engineering
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.404
H-Index - 67
eISSN - 1939-019X
pISSN - 0008-4034
DOI - 10.1002/cjce.5450520226
Subject(s) - carbon dioxide , isothermal process , thermodynamics , binary system , vapor–liquid equilibrium , chemistry , vapor pressure , equation of state , binary number , range (aeronautics) , materials science , organic chemistry , physics , arithmetic , mathematics , composite material
Vapor‐liquid equilibrium compositions were measured at four isothermal conditions from −60°F to 60°F over the pressure range from 101.5 to 827.0 psia for the binary system ethane‐carbon dioxide. A forced recirculation apparatus was employed for the determination. The data obtained were found to be thermodynamically consistent, and were compared favorably with the values predicted by means of a modified Redlich‐Kwong equation of state especially at the lower temperatures.
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