The Experts below are selected from a list of 324 Experts worldwide ranked by ideXlab platform
Kenneth R Hall - One of the best experts on this subject based on the ideXlab platform.
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Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + Tert-Butanol, and Isobutanol + Tert-Butanol from (308.15 to 343.15) K
Journal of Chemical & Engineering Data, 2013Co-Authors: Micael G. Bravo-sánchez, Alejandro Estrada-baltazar, Gustavo A. Iglesias-silva, Kenneth R HallAbstract:This paper presents densities and viscosities for binary mixtures of 2-butanol + isobutanol, 2-butanol + Tert-Butanol, and isobutanol + Tert-Butanol at temperatures between (308.15 and 343.15) K ov...
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densities and viscosities of binary mixtures of 2 butanol isobutanol 2 butanol tert butanol and isobutanol tert butanol from 308 15 to 343 15 k
Journal of Chemical & Engineering Data, 2013Co-Authors: Micael G Bravosanchez, Gustavo A Iglesiassilva, Alejandro Estradabaltazar, Kenneth R HallAbstract:This paper presents densities and viscosities for binary mixtures of 2-butanol + isobutanol, 2-butanol + Tert-Butanol, and isobutanol + Tert-Butanol at temperatures between (308.15 and 343.15) K ov...
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densities and viscosities of binary mixtures of n butanol with 2 butanol isobutanol and tert butanol from 303 15 to 343 15 k
Journal of Chemical & Engineering Data, 2010Co-Authors: Micael G Bravosanchez, Gustavo A Iglesiassilva, Alejandro Estradabaltazar, Kenneth R HallAbstract:This paper presents densities and viscosities for n-butanol, 2-butanol, isobutanol, Tert-Butanol, and for binary mixtures with n-butanol as a common component at temperatures between (303.15 and 343.15) K over the entire composition range. The experimental apparatuses are a vibrating-tube densimeter for the density measurements and two Cannon−Fenske viscosimeters for the viscosity measurements. We have calculated excess molar volumes, dynamic viscosities, and excess Gibbs energy of activation from the experimental measurements. A temperature-dependent Redlich−Kister equation represents the calculated excess molar volumes, viscosity deviations, and excess Gibbs energy of activation. The Grunberg−Nissan equation has been used to correlate the experimental kinematic viscosities of the binary liquid mixtures.
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Densities and viscosities of binary mixtures of n -butanol with 2-butanol, isobutanol, and tert -butanol from (303.15 to 343.15) K
Journal of Chemical and Engineering Data, 2010Co-Authors: Micael G. Bravo-sánchez, Alejandro Estrada-baltazar, Gustavo A. Iglesias-silva, Kenneth R HallAbstract:This paper presents densities and viscosities for n-butanol, 2-butanol, isobutanol, Tert-Butanol, and for binary mixtures with n-butanol as a common component at temperatures between (303.15 and 343.15) K over the entire composition range. The experimental apparatuses are a vibrating-tube densimeter for the density measurements and two Cannon-Fenske viscosimeters for the viscosity measurements. We have calculated excess molar volumes, dynamic viscosities, and excess Gibbs energy of activation from the experimental measurements. A temperature-dependent Redlich-Kister equation represents the calculated excess molar volumes, viscosity deviations, and excess Gibbs energy of activation. The Grunberg-Nissan equation has been used to correlate the experimental kinematic viscosities of the binary liquid mixtures. © 2010 American Chemical Society.
Ivan Wichterle - One of the best experts on this subject based on the ideXlab platform.
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Isothermal vapour–liquid equilibrium in the binary Tert-Butanol or 2,2,4-trimethylpentane+1-tert-butoxy-2-propanol, and in the ternary Tert-Butanol+2,2,4-trimethylpentane+1-tert-butoxy-2-propanol systems
Fluid Phase Equilibria, 2001Co-Authors: Svatoslava Bernatová, Ivan WichterleAbstract:Abstract Vapour–liquid equilibrium data are reported for the ternary tert -butanol+2,2,4-trimethylpentane+1- tert -butoxy-2-propanol system and for the binary tert -butanol+1- tert -butoxy-2-propanol and 2,2,4-trimethylpentane+1- tert -butoxy-2-propanol subsystems. The data were measured isothermally at 318.13, 328.20, and 339.28 K covering pressure range 3–100 kPa. The binary vapour–liquid equilibrium data were correlated using Wilson, NRTL, and Redlich–Kister equations; the parameters obtained were used for calculation of phase behaviour in ternary system and for subsequent comparison with experimental data.
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Isothermal vapour–liquid equilibria in the ternary system tert-butyl methyl ether + Tert-Butanol + 2,2,4-trimethylpentane and the three binary subsystems
Fluid Phase Equilibria, 2001Co-Authors: Svatoslava Bernatová, Ivan WichterleAbstract:Vapour–liquid equilibrium data are reported for the ternary tert-butyl methyl ether + Tert-Butanol + 2, 2, 4-trimethylpentane and the three binary tert-butyl methyl ether + Tert-Butanol, tert-butyl methyl ether + 2,2,4-trimethylpentane, Tert-Butanol + 2,2,4-trimethylpentane subsystems. The data were measured isothermally at 318.13, 328.20, and 339.28 K covering pressure range 15–100 kPa. Azeotropic data are presented for the Tert-Butanol + 2,2,4-trimethylpentane system. Molar excess volumes at 298.15 K are given for the three binary systems. The binary vapour– liquid equilibrium data were correlated using Wilson, NRTL, and Redlich–Kister equations; the parameters obtained were used for calculation of phase behaviour in ternary system and for subsequent comparison with experimental data. © 2001 Elsevier Science B.V. All rights reserved.
Micael G Bravosanchez - One of the best experts on this subject based on the ideXlab platform.
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densities and viscosities of binary mixtures of 2 butanol isobutanol 2 butanol tert butanol and isobutanol tert butanol from 308 15 to 343 15 k
Journal of Chemical & Engineering Data, 2013Co-Authors: Micael G Bravosanchez, Gustavo A Iglesiassilva, Alejandro Estradabaltazar, Kenneth R HallAbstract:This paper presents densities and viscosities for binary mixtures of 2-butanol + isobutanol, 2-butanol + Tert-Butanol, and isobutanol + Tert-Butanol at temperatures between (308.15 and 343.15) K ov...
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densities and viscosities of binary mixtures of n butanol with 2 butanol isobutanol and tert butanol from 303 15 to 343 15 k
Journal of Chemical & Engineering Data, 2010Co-Authors: Micael G Bravosanchez, Gustavo A Iglesiassilva, Alejandro Estradabaltazar, Kenneth R HallAbstract:This paper presents densities and viscosities for n-butanol, 2-butanol, isobutanol, Tert-Butanol, and for binary mixtures with n-butanol as a common component at temperatures between (303.15 and 343.15) K over the entire composition range. The experimental apparatuses are a vibrating-tube densimeter for the density measurements and two Cannon−Fenske viscosimeters for the viscosity measurements. We have calculated excess molar volumes, dynamic viscosities, and excess Gibbs energy of activation from the experimental measurements. A temperature-dependent Redlich−Kister equation represents the calculated excess molar volumes, viscosity deviations, and excess Gibbs energy of activation. The Grunberg−Nissan equation has been used to correlate the experimental kinematic viscosities of the binary liquid mixtures.
Svatoslava Bernatová - One of the best experts on this subject based on the ideXlab platform.
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Isothermal vapour–liquid equilibrium in the binary Tert-Butanol or 2,2,4-trimethylpentane+1-tert-butoxy-2-propanol, and in the ternary Tert-Butanol+2,2,4-trimethylpentane+1-tert-butoxy-2-propanol systems
Fluid Phase Equilibria, 2001Co-Authors: Svatoslava Bernatová, Ivan WichterleAbstract:Abstract Vapour–liquid equilibrium data are reported for the ternary tert -butanol+2,2,4-trimethylpentane+1- tert -butoxy-2-propanol system and for the binary tert -butanol+1- tert -butoxy-2-propanol and 2,2,4-trimethylpentane+1- tert -butoxy-2-propanol subsystems. The data were measured isothermally at 318.13, 328.20, and 339.28 K covering pressure range 3–100 kPa. The binary vapour–liquid equilibrium data were correlated using Wilson, NRTL, and Redlich–Kister equations; the parameters obtained were used for calculation of phase behaviour in ternary system and for subsequent comparison with experimental data.
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Isothermal vapour–liquid equilibria in the ternary system tert-butyl methyl ether + Tert-Butanol + 2,2,4-trimethylpentane and the three binary subsystems
Fluid Phase Equilibria, 2001Co-Authors: Svatoslava Bernatová, Ivan WichterleAbstract:Vapour–liquid equilibrium data are reported for the ternary tert-butyl methyl ether + Tert-Butanol + 2, 2, 4-trimethylpentane and the three binary tert-butyl methyl ether + Tert-Butanol, tert-butyl methyl ether + 2,2,4-trimethylpentane, Tert-Butanol + 2,2,4-trimethylpentane subsystems. The data were measured isothermally at 318.13, 328.20, and 339.28 K covering pressure range 15–100 kPa. Azeotropic data are presented for the Tert-Butanol + 2,2,4-trimethylpentane system. Molar excess volumes at 298.15 K are given for the three binary systems. The binary vapour– liquid equilibrium data were correlated using Wilson, NRTL, and Redlich–Kister equations; the parameters obtained were used for calculation of phase behaviour in ternary system and for subsequent comparison with experimental data. © 2001 Elsevier Science B.V. All rights reserved.
Gustavo A Iglesiassilva - One of the best experts on this subject based on the ideXlab platform.
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densities and viscosities of binary mixtures of 2 butanol isobutanol 2 butanol tert butanol and isobutanol tert butanol from 308 15 to 343 15 k
Journal of Chemical & Engineering Data, 2013Co-Authors: Micael G Bravosanchez, Gustavo A Iglesiassilva, Alejandro Estradabaltazar, Kenneth R HallAbstract:This paper presents densities and viscosities for binary mixtures of 2-butanol + isobutanol, 2-butanol + Tert-Butanol, and isobutanol + Tert-Butanol at temperatures between (308.15 and 343.15) K ov...
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densities and viscosities of binary mixtures of n butanol with 2 butanol isobutanol and tert butanol from 303 15 to 343 15 k
Journal of Chemical & Engineering Data, 2010Co-Authors: Micael G Bravosanchez, Gustavo A Iglesiassilva, Alejandro Estradabaltazar, Kenneth R HallAbstract:This paper presents densities and viscosities for n-butanol, 2-butanol, isobutanol, Tert-Butanol, and for binary mixtures with n-butanol as a common component at temperatures between (303.15 and 343.15) K over the entire composition range. The experimental apparatuses are a vibrating-tube densimeter for the density measurements and two Cannon−Fenske viscosimeters for the viscosity measurements. We have calculated excess molar volumes, dynamic viscosities, and excess Gibbs energy of activation from the experimental measurements. A temperature-dependent Redlich−Kister equation represents the calculated excess molar volumes, viscosity deviations, and excess Gibbs energy of activation. The Grunberg−Nissan equation has been used to correlate the experimental kinematic viscosities of the binary liquid mixtures.