UB Paderborn / Katalog / Suche / in CDI

Estimation of Thermal Conductivities for Binary and Ternary Liquid Mixtures Using Excess Thermal Conductivity Model

Journal of solution chemistry, 2023-01, Vol.52 (1), p.105-133

2023

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Estimation of Ionic Conductivity and Viscosity of Ionic Liquids Using a QSPR Model

Journal of physical chemistry. C, 2007-11, Vol.111 (43), p.15989-15994

2007

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Evaluation of Solid–Liquid Equilibria for Ternary Pharmaceutical Compound + Water + Cyclodextrin or Its Derivative Systems with Wilson and Modified Chrastil Models

Journal of chemical engineering of Japan, 2023, Vol.56 (1)

2023

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Estimation of kinematic viscosities at high pressures for binary mixtures CO2 + solvent using modified Eyring-Wilson and McAllister models

Molecular physics, 2019-12, Vol.117 (23-24), p.3913-3921

2019

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Estimation of kinematic viscosities for CO2 expanded liquids by ASOG-VISCO model

Fluid phase equilibria, 2018-08, Vol.470, p.188-192

2018

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Determination and prediction of solubilities of active pharmaceutical ingredients in selected organic solvents

Fluid phase equilibria, 2015-11, Vol.406, p.116-123

2015

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Vapor-liquid equilibrium (VLE) measurements of ethanol – heptane at isothermal (363.15, 393.15 and 423.15 K) and isobaric (101.33 kPa) conditions and correlation of liquid viscosity data

Chemical thermodynamics and thermal analysis, 2022-06, Vol.6, p.100041, Article 100041

2022

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Influence of sulfate-based anion ionic liquids on the separation factor of the binary azeotropic system acetone+methanol

Fluid phase equilibria, 2013-02, Vol.340, p.27-30

2013

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Selection of entrainers for the separation of the binary azeotropic system methanol + dimethyl carbonate by extractive distillation

Fluid phase equilibria, 2011-11, Vol.310 (1), p.166-181

2011

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Measurement and correlation of solubilities of the poorly water-soluble pharmaceutical compound etodolac by addition of co-solvents

Fluid phase equilibria, 2013-11, Vol.357, p.43-49

2013

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Ebulliometric Determination and Prediction of Vapor–Liquid Equilibria for Binary Mixtures of Ethanol and Ethyl Hexanoate

Journal of chemical and engineering data, 2011-12, Vol.56 (12), p.5045-5051

2011

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Estimation of kinematic viscosities and thermal conductivities for liquid mixtures using ASOG-VLE, ASOG-VISCO and ASOG-ThermConduct models

Fluid phase equilibria, 2023-02, Vol.565, p.113668, Article 113668

2023

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Solubilities of Salicylic Acid in Pure Solvents and Binary Mixtures Containing Cosolvent

Journal of chemical and engineering data, 2009-02, Vol.54 (2), p.480-484

2009

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Determination and correlation of solubilities of famotidine in water + co-solvent mixed solvents

Fluid phase equilibria, 2011-03, Vol.302 (1), p.115-122

2011

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Isobaric vapor–liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME + PGMEA at reduced pressures

Fluid phase equilibria, 2007-10, Vol.260 (1), p.65-69

2007

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Excess molar enthalpies in the binary system of carbon dioxide + ethyl lactate at 298.15 and 303.15 K and 5.0–7.0 MPa

Fluid phase equilibria, 2023-09, Vol.572, p.113838, Article 113838

2023

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Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethylether, Chloroethane, 1,1-Difluoroethane, and Hexane in Tetrahydropyran

Journal of chemical and engineering data, 2007-11, Vol.52 (6), p.2245-2249

2007

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Fish-shaped diagram of liquid–liquid equilibria for the mixtures water + n-alkane + n-alkyl polyglycol ether

Fluid phase equilibria, 2022-08, Vol.559, p.113492, Article 113492

2022

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Vapor-liquid equilibria for binary systems carbon dioxide + 1,1,1,2,3,3-hexafluoro-3-(2,2,2-trifluoroethoxy)propane or 1-ethoxy-1,1,2,2,3,3,4,4,4-nonafluorobutane at 303.15–323.15 K

Fluid phase equilibria, 2020-12, Vol.524, p.112814, Article 112814

2020

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Solid–liquid equilibria for selected binary systems containing diphenyl carbonate

Fluid phase equilibria, 2019-01, Vol.479, p.17-24

2019

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Isobaric Vapor–Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems

Journal of chemical and engineering data, 2012-02, Vol.57 (2), p.339-344

2012

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Estimation of kinematic viscosities for multi-component systems using modified Eyring and activity coefficient model

Fluid phase equilibria, 2019-07, Vol.492, p.137-144

2019

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Excess molar enthalpies of the binary system carbon dioxide + butyl levulinate at 298.15 and 303.15 K and 5.0–7.0 MPa

Fluid phase equilibria, 2019-12, Vol.502, p.112288, Article 112288

2019

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Estimation of kinematic viscosities at high pressures for binary mixtures CO 2 + solvent using modified Eyring–Wilson and McAllister models

Molecular physics, 2019-12, Vol.117 (23-24), p.3913-3921

2019

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Computer-aided reverse design for ionic liquids by QSPR using descriptors of group contribution type for ionic conductivities and viscosities

Fluid phase equilibria, 2007-12, Vol.261 (1), p.434-443

2007

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Estimation of Thermal Conductivities for Binary and Ternary Liquid Mixtures Using Excess Thermal Conductivity Model

Estimation of Ionic Conductivity and Viscosity of Ionic Liquids Using a QSPR Model

Evaluation of Solid–Liquid Equilibria for Ternary Pharmaceutical Compound + Water + Cyclodextrin or Its Derivative Systems with Wilson and Modified Chrastil Models

Estimation of kinematic viscosities at high pressures for binary mixtures CO2 + solvent using modified Eyring-Wilson and McAllister models

Estimation of kinematic viscosities for CO2 expanded liquids by ASOG-VISCO model

Determination and prediction of solubilities of active pharmaceutical ingredients in selected organic solvents

Vapor-liquid equilibrium (VLE) measurements of ethanol – heptane at isothermal (363.15, 393.15 and 423.15 K) and isobaric (101.33 kPa) conditions and correlation of liquid viscosity data

Influence of sulfate-based anion ionic liquids on the separation factor of the binary azeotropic system acetone+methanol

Selection of entrainers for the separation of the binary azeotropic system methanol + dimethyl carbonate by extractive distillation

Measurement and correlation of solubilities of the poorly water-soluble pharmaceutical compound etodolac by addition of co-solvents

Ebulliometric Determination and Prediction of Vapor–Liquid Equilibria for Binary Mixtures of Ethanol and Ethyl Hexanoate

Estimation of kinematic viscosities and thermal conductivities for liquid mixtures using ASOG-VLE, ASOG-VISCO and ASOG-ThermConduct models

Solubilities of Salicylic Acid in Pure Solvents and Binary Mixtures Containing Cosolvent

Determination and correlation of solubilities of famotidine in water + co-solvent mixed solvents

Isobaric vapor–liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME + PGMEA at reduced pressures

Excess molar enthalpies in the binary system of carbon dioxide + ethyl lactate at 298.15 and 303.15 K and 5.0–7.0 MPa

Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethylether, Chloroethane, 1,1-Difluoroethane, and Hexane in Tetrahydropyran

Fish-shaped diagram of liquid–liquid equilibria for the mixtures water + n-alkane + n-alkyl polyglycol ether

Vapor-liquid equilibria for binary systems carbon dioxide + 1,1,1,2,3,3-hexafluoro-3-(2,2,2-trifluoroethoxy)propane or 1-ethoxy-1,1,2,2,3,3,4,4,4-nonafluorobutane at 303.15–323.15 K

Solid–liquid equilibria for selected binary systems containing diphenyl carbonate

Isobaric Vapor–Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems

Estimation of kinematic viscosities for multi-component systems using modified Eyring and activity coefficient model

Excess molar enthalpies of the binary system carbon dioxide + butyl levulinate at 298.15 and 303.15 K and 5.0–7.0 MPa

Estimation of kinematic viscosities at high pressures for binary mixtures CO 2 + solvent using modified Eyring–Wilson and McAllister models

Computer-aided reverse design for ionic liquids by QSPR using descriptors of group contribution type for ionic conductivities and viscosities

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