Vapour-liquid equilibria for the carbon dioxide and carvacrol system at elevated pressures

Gary Leeke; Regina Santos; MB King

doi:10.1021/je000342k

Vapour-liquid equilibria for the carbon dioxide and carvacrol system at elevated pressures

Gary Leeke, Regina Santos, MB King

Chemical Engineering

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25 Citations (Scopus)

Abstract

Vapor-liquid equilibria data were measured for the first time for the carbon dioxide + carvacrol system at 313 K from 0.4 to 30.8 MPa and at 323 K from 0.3 to 30.0 MPa. Data were obtained using a circulation-type apparatus at sufficiently high fluid densities and a continuous flow-type apparatus at low fluid densities. The results were correlated by the Peng-Robinson equation of state and by Zudkevitch's modification to the Redlich-Kwong equation of state, using in both cases classical mixing rules with one adjustable parameter.

Original language	English
Pages (from-to)	541
Number of pages	1
Journal	Journal of Chemical Engineering Data
Volume	46
DOIs	https://doi.org/10.1021/je000342k
Publication status	Published - 1 Jan 2001

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abstract = "Vapor-liquid equilibria data were measured for the first time for the carbon dioxide + carvacrol system at 313 K from 0.4 to 30.8 MPa and at 323 K from 0.3 to 30.0 MPa. Data were obtained using a circulation-type apparatus at sufficiently high fluid densities and a continuous flow-type apparatus at low fluid densities. The results were correlated by the Peng-Robinson equation of state and by Zudkevitch's modification to the Redlich-Kwong equation of state, using in both cases classical mixing rules with one adjustable parameter.",

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N2 - Vapor-liquid equilibria data were measured for the first time for the carbon dioxide + carvacrol system at 313 K from 0.4 to 30.8 MPa and at 323 K from 0.3 to 30.0 MPa. Data were obtained using a circulation-type apparatus at sufficiently high fluid densities and a continuous flow-type apparatus at low fluid densities. The results were correlated by the Peng-Robinson equation of state and by Zudkevitch's modification to the Redlich-Kwong equation of state, using in both cases classical mixing rules with one adjustable parameter.

AB - Vapor-liquid equilibria data were measured for the first time for the carbon dioxide + carvacrol system at 313 K from 0.4 to 30.8 MPa and at 323 K from 0.3 to 30.0 MPa. Data were obtained using a circulation-type apparatus at sufficiently high fluid densities and a continuous flow-type apparatus at low fluid densities. The results were correlated by the Peng-Robinson equation of state and by Zudkevitch's modification to the Redlich-Kwong equation of state, using in both cases classical mixing rules with one adjustable parameter.

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Vapour-liquid equilibria for the carbon dioxide and carvacrol system at elevated pressures

Abstract

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