Keywords: مدل ویلسون; Vapor-liquid equilibria; Water activity; Poly (ethylene glycol); Dipotassium tartrate; Wilson model;
مقالات ISI مدل ویلسون (ترجمه نشده)
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Keywords: مدل ویلسون; Erodibility; Excess shear stress model; Fluvial resistance; Streambank erosion; Wilson model
Keywords: مدل ویلسون; n-Alkane; Methyl myristate; VLE; NRTL model; UNIQUAC model; Wilson model
Commentary concerning “measurement and correlation of solubility and solution thermodynamics of 1,3-dimethylurea in different solvents from Tâ¯=â¯(288.15 to 328.15) K”
Keywords: مدل ویلسون; 1,3-Dimethylurea; Solubility; Wilson model;
Isobaric (vapor + liquid) equilibria for 2-methylthiophene with n-heptane, 2,2,4-trimethylpentane, n-nonane and n-decane at 90.00 kPa
Keywords: مدل ویلسون; Vapor-liquid equilibrium; 2-Methylthiophene; Wilson model; NRTL model; Original UNIFAC model;
Measurement and correlation of solubility of 4-chloro-2,5-dimethoxynitrobenzene and 4-chloro-2,5-dimethoxyaniline in methanol, ethanol, xylene and toluene
Keywords: مدل ویلسون; 4-Chloro-2,5-dimethoxynitrobenzene; 4-Chloro-2,5-dimethoxyaniline; Solubility; Wilson model; NRTL model
Isobaric vapor–liquid equilibrium of the binary system sec-butyl acetate + para-xylene and the quaternary system methyl acetate + para-xylene + sec-butyl acetate + acetic acid at 101.3 kPa
Keywords: مدل ویلسون; VLE, vapor–liquid equilibrium; NRTL, non-random two liquid; UNIQUAC, universal quasi chemical; RMSD, root mean square deviationsec-Butyl acetate; para-Xylene; NRTL model; Wilson model; UNIQUAC model
Isobaric vapor–liquid equilibrium for binary system of 2-ethylthiophene + n-octane at 101.33 kPa
Keywords: مدل ویلسون; Vapor–liquid equilibrium; 2-Ethylthiophene; Wilson model; NRTL model; UNIQUAC model
Isobaric vapor–liquid equilibrium for binary system of cinnamaldehyde + benzaldehyde at 10, 20 and 30 kPa
Keywords: مدل ویلسون; Vapor–liquid equilibrium (VLE); Cinnamaldehyde; Benzaldehyde; NRTL model; Wilson model; UNIFAC model
Isobaric vapor–liquid equilibria of the binary mixtures propylene glycol methyl ether + propylene glycol methyl ether acetate, methyl acetate + propylene glycol methyl ether and methanol + propylene glycol methyl ether acetate at 101.3 kPa
Keywords: مدل ویلسون; Vapor–liquid equilibrium; Propylene glycol methyl ether; Propylene glycol methyl ether acetate; NRTL model; Wilson model
Ebulliometric determination of vapor-liquid equilibria for binary mixtures of NMP with some cyclic compounds
Keywords: مدل ویلسون; Vapor-liquid equilibrium; Ebulliometer; Activity coefficients; Wilson model; Gibbs energy;
Isobaric (vapour + liquid) equilibria for three binary systems (toluene + anisole, n-butylbenzene + anisole, and guaiacol + anisole) at 101.33 kPa
Keywords: مدل ویلسون; Anisole; VLE; NRTL model; UNIQUAC model; Wilson model
Isobaric vapor–liquid equilibria of the binary system acetone + acetone oxime methyl ether at 101.3 kPa
Keywords: مدل ویلسون; Vapor–liquid equilibria data; Acetone; Acetone oxime methyl ether; NRTL model; Wilson model
Experimental determination and activity coefficient based models for mixture solubilities of nitrophenol isomers in supercritical carbon dioxide
Keywords: مدل ویلسون; Non-ideal mixtures; Activity coefficient; Cosolute; Wilson model; NRTL model
Isobaric vapor–liquid equilibrium for four binary systems of 3-methylthiophene
Keywords: مدل ویلسون; Vapor–liquid equilibrium; 3-Methylthiophene; Wilson model; UNIFAC model; UNIFAC-Dortmund model
Vapor–liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Keywords: مدل ویلسون; Activity coefficients; Wilson model; Gibb's energy; Excess molar volume; Inter molecular hydrogen bonding
Isobaric vapor–liquid equilibrium for four binary systems of thiophene
Keywords: مدل ویلسون; Thiophene; Vapor–liquid equilibrium; Activity coefficients; Wilson model; UNIFAC model
Microstructure and sound absorption of snow
Keywords: مدل ویلسون; Acoustic; Snow; Microtomography; Sound absorption; Minkowski functionals; Wilson model; Permeability
Solubility of decanedioic acid in binary solvent mixtures
Keywords: مدل ویلسون; Decanedioic acid; Solubility; Synergistic effect; NRTL model; Wilson model
Experimental (vapour + liquid) equilibrium data of (methanol + water), (water + glycerol) and (methanol + glycerol) systems at atmospheric and sub-atmospheric pressures
Keywords: مدل ویلسون; (Vapour + liquid) equilibrium; Glycerol; Methanol; Water; Wilson model
Experimental measurements and correlations of vapor–liquid equilibrium data for the binary system of chloroform + N,N-dimethylformamide at 101.3 kPa
Keywords: مدل ویلسون; N,N-dimethylformamide; Chloroform; VLE; NRTL model; UNIQUAC model; Wilson model
Excess molar volumes and excess molar enthalpies of binary mixtures for 1,2-dichloropropane + 2-alkoxyethanol acetates at 298.15 K
Keywords: مدل ویلسون; Excess molar volumes; Excess molar enthalpies; 1,2-Dichloropropane; 2-Alkoxyethanol acetate; Redlich–Kister equation; Wilson model; NRTL model; UNIQUAC model
Bubble temperature measurements on seven binary mixtures formed by ethylbenzene at 94.7 kPa
Keywords: مدل ویلسون; Bubble temperatures; Wilson model; Ethylbenzene; Vapor + liquid equilibria;
Activity coefficients in binary mixtures formed by cyclohexanone with a variety of compounds at 94.7Â kPa
Keywords: مدل ویلسون; Wilson model; Activity coefficients; Cyclohexanone; Acrylonitrile; Pyrazines; Cyclohexane; Carbontetrachloride;
Excess molar enthalpies of methyl isobutyl ketone (MIBK) with alkan-1-ols (C1-C6) and their correlations at 298.15Â K
Keywords: مدل ویلسون; Excess enthalpies; Alkan-1-ols; Methyl isobutyl ketone (MIBK); Wilson model; NRTL model;
Uncertainties in parameter estimation and optimal control in batch distillation
Keywords: مدل ویلسون; Batch distillation; Optimal control; Ito processes; Time-dependent uncertainties; Thermodynamic models; Wilson model; Interval-Newton method;