Liquid−Liquid Equilibrium for the System Water + 1,4-Dioxane + 2,6-Dimethyloct-7-en-2-ol over the Temperature Range of (343.2 to 358.2) K

Journal of Chemical & Engineering Data ◽

10.1021/je900366m ◽

2010 ◽

Vol 55 (1) ◽

pp. 558-560 ◽

Author(s):

Biyu Wang ◽

Ting Qiu ◽

Sujuan Li

Keyword(s):

Liquid Equilibrium ◽

Temperature Range ◽

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Liquid−Liquid Equilibrium and Critical Phenomena in the Ternary System Water + 2-Methoxyethanol + Toluene in the Temperature Range 283 K to 383 K

Journal of Chemical & Engineering Data ◽

10.1021/je025544q ◽

2002 ◽

Vol 47 (5) ◽

pp. 1303-1306 ◽

Author(s):

Dmitry G. Cherkasov ◽

Konstantin K. Ilin

Keyword(s):

Ternary System ◽

Critical Phenomena ◽

Liquid Equilibrium ◽

Temperature Range ◽

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Liquid–liquid equilibrium for the system water+1,4-dioxane+cyclohexanol over the temperature range of 313.2–343.2K

Fluid Phase Equilibria ◽

10.1016/j.fluid.2012.03.010 ◽

2012 ◽

Vol 324 ◽

pp. 28-32 ◽

Author(s):

Ting Qiu ◽

Xiao-da Wang ◽

Hui Tian ◽

Zhi-xian Huang

Keyword(s):

Liquid Equilibrium ◽

Temperature Range ◽

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Liquid−Liquid Equilibrium for the System Water + Cyclohexene + Cyclohexanol over the Temperature Range of (303.2 to 403.2) K

Journal of Chemical & Engineering Data ◽

10.1021/je900886s ◽

2010 ◽

Vol 55 (7) ◽

pp. 2529-2531 ◽

Author(s):

Biyu Wang ◽

Xiuxiu Ge ◽

Huidong Zheng ◽

Ting Qiu ◽

Yanxiang Wu

Keyword(s):

Liquid Equilibrium ◽

Temperature Range ◽

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Quaternary isobaric (vapor+liquid+liquid) equilibrium and (vapor+liquid) equilibrium for the system (water+ethanol+cyclohexane+heptane) at 101.3kPa

The Journal of Chemical Thermodynamics ◽

10.1016/j.jct.2011.02.016 ◽

2011 ◽

Vol 43 (8) ◽

pp. 1097-1103 ◽

Author(s):

Ana Pequenín ◽

Juan Carlos Asensi ◽

Vicente Gomis

Keyword(s):

Liquid Equilibrium ◽

Vapor Liquid Equilibrium ◽

System Water ◽

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Density, Viscosity, and Vapor–Liquid Equilibrium of the Ternary System Water–1-Ethyl-3-methylimidazolium Acetate–1-Ethyl-3-Methylimidazolium Trifluoromethanesulfonate

Journal of Chemical & Engineering Data ◽

10.1021/acs.jced.6b00801 ◽

2017 ◽

Vol 62 (2) ◽

pp. 720-728 ◽

Author(s):

Markus Bücherl ◽

Fabian Hardock ◽

Elisa Kaiser ◽

Andreas Netsch ◽

Karlheinz Schaber

Keyword(s):

Ternary System ◽

Liquid Equilibrium ◽

Vapor Liquid Equilibrium ◽

System Water ◽

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Liquid−Liquid Equilibrium for the System Heptane +o-Xylene + Diethylene Glycol over the Temperature Range of 288.15 K to 318.15 K

Journal of Chemical & Engineering Data ◽

10.1021/je049601m ◽

2005 ◽

Vol 50 (3) ◽

pp. 924-927 ◽

Author(s):

Ibrahim Ashour ◽

Mohamed A. Abdulkarim

Keyword(s):

Diethylene Glycol ◽

Liquid Equilibrium ◽

Temperature Range

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Liquid–liquid equilibrium of the ternary system water+acetic acid+sec-butyl acetate

Fluid Phase Equilibria ◽

10.1016/j.fluid.2010.01.005 ◽

2010 ◽

Vol 293 (1) ◽

pp. 73-78 ◽

Author(s):

Song Hu ◽

Qing-lin Chen ◽

Bing-jian Zhang ◽

Yuan-lan Liang ◽

Xue-nong Gao

Keyword(s):

Acetic Acid ◽

Ternary System ◽

Butyl Acetate ◽

Liquid Equilibrium ◽

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Isobaric Vapor−Liquid−Liquid Equilibrium and Vapor−Liquid Equilibrium for the Quaternary System Water−Ethanol−Cyclohexane−Isooctane at 101.3 kPa

Journal of Chemical & Engineering Data ◽

10.1021/je900604a ◽

2010 ◽

Vol 55 (3) ◽

pp. 1227-1231 ◽

Author(s):

Ana Pequenín ◽

Juan Carlos Asensi ◽

Vicente Gomis

Keyword(s):

Quaternary System ◽

Liquid Equilibrium ◽

Vapor Liquid Equilibrium ◽

System Water ◽

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Liquid-liquid equilibrium data for the ternary system water-isopropyl alcohol-ethylbenzene at 25°

Journal of Applied Chemistry ◽

10.1002/jctb.5010171206 ◽

2007 ◽

Vol 17 (12) ◽

pp. 361-363

Author(s):

E. T. Knypl ◽

S. Z. Wojdylo

Keyword(s):

Ternary System ◽

Isopropyl Alcohol ◽

Liquid Equilibrium ◽

Equilibrium Data ◽

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Verdampfungsgleichgewicht und thermodynamisehe Funktionen des flüssigen Systems Wasser + Essigsäure / Vapour-Liquid. Equilibrium and Thermodynamic Functions of the Liquid System Water + Acetic Acid

Zeitschrift für Naturforschung A ◽

10.1515/zna-1973-1029 ◽

1973 ◽

Vol 28 (10) ◽

pp. 1740-1742 ◽

Author(s):

R. Haase ◽

M. Pehlke ◽

K.-H. Dücker

Keyword(s):

Acetic Acid ◽

Composition Dependence ◽

Excess Enthalpy ◽

Excess Entropy ◽

Liquid System ◽

Gibbs Function ◽

Liquid Equilibrium ◽

Molar Excess ◽

C 30 ◽

Vapour pressures and vapour compositions of the liquid system water + acetic acid have been measured at 25 °C, 30 °C, 35 °C, 40 °C, and 45 °C in the whole range of compositions. The dimerization of acetic acid in the vapour being taken into account, the molar excess Gibbs function ḠE is derived from the measurements. Earlier measurements of the molar excess enthalpy HE are combined with the -GE values to give the molar excess entropy SE. The “symmetry rule” (Haase, 1951) concerning the composition dependence of ḠE, -HE, and S̄E has been confirmed.

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