Vapor-Liquid Equilibria in the System of Toluene/Aniline, Aniline/Naphthalene, and Naphthalene/Quinoline

Changa Ha Lee; Quen Chen; Rahoma S. Mohamed; Gerald D. Holder

doi:10.1021/je00006a011

Vapor-Liquid Equilibria in the System of Toluene/Aniline, Aniline/Naphthalene, and Naphthalene/Quinoline

Changa Ha Lee, Quen Chen, Rahoma S. Mohamed, Gerald D. Holder

Department of Chemical and Biomolecular Engineering

Research output: Contribution to journal › Article › peer-review

7 Citations (Scopus)

Abstract

Vapor-liquid equilibria for the aniline/naphthalene, toluene/aniline, and naphthalene/quinoline systems have been determined at 0-1500 kPa and 490-623 K by using a static equilibrium cell. The data can be accurately correlated with the modified Peng-Roblnson equation of state by using density-dependent mixing rules. The binary interaction parameters and correction factors for the equation of state are reported at each isotherm. The presence of coal-derived solids in these binary systems did not influence any of the binary bubble pressures.

Original language	English
Pages (from-to)	179-183
Number of pages	5
Journal	Journal of Chemical and Engineering Data
Volume	37
Issue number	2
DOIs	https://doi.org/10.1021/je00006a011
Publication status	Published - 1992 Apr 1

All Science Journal Classification (ASJC) codes

Chemistry(all)
Chemical Engineering(all)

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10.1021/je00006a011

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abstract = "Vapor-liquid equilibria for the aniline/naphthalene, toluene/aniline, and naphthalene/quinoline systems have been determined at 0-1500 kPa and 490-623 K by using a static equilibrium cell. The data can be accurately correlated with the modified Peng-Roblnson equation of state by using density-dependent mixing rules. The binary interaction parameters and correction factors for the equation of state are reported at each isotherm. The presence of coal-derived solids in these binary systems did not influence any of the binary bubble pressures.",

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AU - Chen, Quen

AU - Mohamed, Rahoma S.

AU - Holder, Gerald D.

PY - 1992/4/1

Y1 - 1992/4/1

N2 - Vapor-liquid equilibria for the aniline/naphthalene, toluene/aniline, and naphthalene/quinoline systems have been determined at 0-1500 kPa and 490-623 K by using a static equilibrium cell. The data can be accurately correlated with the modified Peng-Roblnson equation of state by using density-dependent mixing rules. The binary interaction parameters and correction factors for the equation of state are reported at each isotherm. The presence of coal-derived solids in these binary systems did not influence any of the binary bubble pressures.

AB - Vapor-liquid equilibria for the aniline/naphthalene, toluene/aniline, and naphthalene/quinoline systems have been determined at 0-1500 kPa and 490-623 K by using a static equilibrium cell. The data can be accurately correlated with the modified Peng-Roblnson equation of state by using density-dependent mixing rules. The binary interaction parameters and correction factors for the equation of state are reported at each isotherm. The presence of coal-derived solids in these binary systems did not influence any of the binary bubble pressures.

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Vapor-Liquid Equilibria in the System of Toluene/Aniline, Aniline/Naphthalene, and Naphthalene/Quinoline

Abstract

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