Liquid−Liquid Equilibrium of Ternary Mixtures Formed by Some Oligooxaethylenes with Ethanol and Hexadecane†

Teresa Treszczanowicz; Andrzej J. Treszczanowicz

doi:10.1021/je800503d

Liquid−Liquid Equilibrium of Ternary Mixtures Formed by Some Oligooxaethylenes with Ethanol and Hexadecane†

Journal of Chemical & Engineering Data ◽

10.1021/je800503d ◽

2009 ◽

Vol 54 (2) ◽

pp. 555-558 ◽

Cited By ~ 1

Author(s):

Teresa Treszczanowicz ◽

Andrzej J. Treszczanowicz

Keyword(s):

Ternary Mixtures ◽

Liquid Equilibrium

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Properties of Refrigerants from Cubic Equations of State

Revista de Chimie ◽

10.37358/rc.08.5.1827 ◽

2008 ◽

Vol 59 (5) ◽

Author(s):

Viorel Feroiu ◽

Dan Geana ◽

Catinca Secuianu

Keyword(s):

Experimental Data ◽

Vapor Pressure ◽

Equations Of State ◽

Ternary Mixtures ◽

Volumetric Properties ◽

Mixing Rules ◽

Saturation Curve ◽

Equilibrium Thermodynamic ◽

Liquid Equilibrium ◽

Binary And Ternary Mixtures

Vapour � liquid equilibrium, thermodynamic and volumetric properties were predicted for three pure hydrofluorocarbons: difluoromethane (R32), pentafluoroethane (R125) and 1,1,1,2 � tetrafluoroethane (R134a) as well as for binary and ternary mixtures of these refrigerants. Three cubic equations of state GEOS3C, SRK (Soave � Redlich � Kwong) and PR (Peng � Robinson) were used. A wide comparison with literature experimental data was made. For the refrigerant mixtures, classical van der Waals mixing rules without interaction parameters were used. The GEOS3C equation, with three parameters estimated by matching several points on the saturation curve (vapor pressure and corresponding liquid volumes), compares favorably to other equations in literature, being simple enough for applications.

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Solid–liquid equilibrium in ternary mixtures of ethyl oleate, ethyl laurate and ethyl palmitate

Fluid Phase Equilibria ◽

10.1016/j.fluid.2012.11.030 ◽

2013 ◽

Vol 339 ◽

pp. 58-66 ◽

Cited By ~ 18

Author(s):

Maria Dolores Robustillo ◽

Deise Fernanda Barbosa ◽

Antonio José de Almeida Meirelles ◽

Pedro de Alcântara Pessôa Filho

Keyword(s):

Ethyl Oleate ◽

Ternary Mixtures ◽

Liquid Equilibrium ◽

Ethyl Palmitate ◽

Solid Liquid

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Isothermal vapor–liquid equilibrium at T=333.15K and excess volumes and molar refractivity deviation at T=298.15K for the ternary mixtures {di-methyl carbonate (DMC)+ethanol+benzene} and {DMC+ethanol+toluene}

Fluid Phase Equilibria ◽

10.1016/j.fluid.2011.01.007 ◽

2011 ◽

Vol 303 (2) ◽

pp. 150-156 ◽

Cited By ~ 11

Author(s):

In-Chan Hwang ◽

So-Jin Park ◽

Kyu-Jin Han

Keyword(s):

Excess Volumes ◽

Ternary Mixtures ◽

Liquid Equilibrium ◽

Vapor Liquid Equilibrium ◽

Molar Refractivity ◽

Methyl Carbonate ◽

Vapor Liquid

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Liquid-liquid equilibrium data measurement and thermodynamic modelling for ternary mixtures composed of water, diethylene glycol dimethyl ether and different solvents at 298.2 K

The Journal of Chemical Thermodynamics ◽

10.1016/j.jct.2021.106669 ◽

2021 ◽

pp. 106669

Author(s):

Yueyang Jiang ◽

Song Lin ◽

Houchun Yan ◽

Hongyue Guo ◽

Qingsong Li

Keyword(s):

Dimethyl Ether ◽

Diethylene Glycol ◽

Thermodynamic Modelling ◽

Ternary Mixtures ◽

Liquid Equilibrium ◽

Glycol Dimethyl Ether ◽

Data Measurement ◽

Equilibrium Data ◽

Diethylene Glycol Dimethyl Ether

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Solid–liquid equilibrium in ternary mixtures of ethyl laurate, ethyl palmitate and ethyl stearate

Fluid Phase Equilibria ◽

10.1016/j.fluid.2013.08.024 ◽

2013 ◽

Vol 358 ◽

pp. 272-281 ◽

Cited By ~ 14

Author(s):

Maria Dolores Robustillo ◽

Deise Fernanda Barbosa ◽

Antonio José de Almeida Meirelles ◽

Pedro de Alcântara Pessôa Filho

Keyword(s):

Ternary Mixtures ◽

Liquid Equilibrium ◽

Ethyl Stearate ◽

Ethyl Palmitate ◽

Solid Liquid

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Isothermal vapor liquid equilibrium measurements for difluoromethane (R32) + fluoroethane (R161) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E)) ternary mixtures

International Journal of Refrigeration ◽

10.1016/j.ijrefrig.2017.04.019 ◽

2017 ◽

Vol 79 ◽

pp. 49-56 ◽

Cited By ~ 6

Author(s):

Xiaozhen Hu ◽

Tao Yang ◽

Xianyang Meng ◽

Jiangtao Wu

Keyword(s):

Ternary Mixtures ◽

Liquid Equilibrium ◽

Vapor Liquid Equilibrium ◽

Vapor Liquid

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Thermodynamics of Octane-Enhancing Additives in Gasolines: Vapor−Liquid Equilibrium of Ternary Mixtures Containing Di-isopropyl Ether or Cyclohexane and 1-Hexene + Benzene at 313.15 K

Journal of Chemical & Engineering Data ◽

10.1021/je0102210 ◽

2002 ◽

Vol 47 (2) ◽

pp. 316-321 ◽

Cited By ~ 10

Author(s):

César R. Chamorro ◽

José J. Segovia ◽

María C. Martín ◽

Miguel A. Villamañán

Keyword(s):

Ternary Mixtures ◽

Isopropyl Ether ◽

Liquid Equilibrium ◽

Vapor Liquid Equilibrium ◽

Vapor Liquid

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Vapor−Liquid Equilibrium of Binary and Ternary Mixtures Containing Isopropyl Ether, 2-Butanol, and Benzene atT= 313.15 K

Journal of Chemical & Engineering Data ◽

10.1021/je0502896 ◽

2006 ◽

Vol 51 (1) ◽

pp. 148-152 ◽

Cited By ~ 11

Author(s):

Rosa M. Villamañán ◽

M. Carmen Martín ◽

César R. Chamorro ◽

José J. Segovia

Keyword(s):

Ternary Mixtures ◽

Isopropyl Ether ◽

Liquid Equilibrium ◽

Vapor Liquid Equilibrium ◽

Binary And Ternary Mixtures ◽

Vapor Liquid

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99/02439 Thermodynamics of octane-enhancing additives in gasolines: vapor-liquid equilibrium of the ternary mixtures methyl tert-butyl ether + heptane + benzene and methyltertbutyl ether + benzene + 1-hexene at 313.15 K

Fuel and Energy Abstracts ◽

10.1016/s0140-6701(99)98208-5 ◽

1999 ◽

Vol 40 (4) ◽

pp. 257

Keyword(s):

Ternary Mixtures ◽

Methyl Tert Butyl Ether ◽

Liquid Equilibrium ◽

Butyl Ether ◽

Vapor Liquid Equilibrium ◽

Tert Butyl ◽

Vapor Liquid

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Liquid–liquid equilibrium data for ternary mixtures composed of n-hexane, benzene and acetonitrile at (298.15, 308.15, and 318.15)K

Fluid Phase Equilibria ◽

10.1016/j.fluid.2014.01.033 ◽

2014 ◽

Vol 367 ◽

pp. 69-73 ◽

Cited By ~ 5

Author(s):

Shengkai Yang ◽

Yujie Wang ◽

Xinhua Qi ◽

Jiuxia Wang

Keyword(s):

Ternary Mixtures ◽

Liquid Equilibrium ◽

Equilibrium Data

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