Vapor—liquid equilibria in the carbon dioxide-ethane system
作者： T.S. Brown , A.J. Kidnay , E.D. Sloan
DOI: 10.1016/0378-3812(88)80028-1
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摘要: Abstract Vapor—liquid equilibria for the binary system carbon dioxide-ethane were measured at eight temperatures from 207 to 270 K. The data modeled with three equations of state: Peng-Robinson, Soave-Redlich-Kwong, and Fuller modification Soave-Redlich-Kwong. All gave satisfactory results use one interaction parameter. However, parameters varied substantially temperature.
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