Keywords: مدل NRTL; Liquid-liquid equilibrium; Phosphoric acid; NRTL model; UNIQUAC model;
مقالات ISI مدل NRTL (ترجمه نشده)
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Keywords: مدل NRTL; Sustainable production; Green solvent; Brazilian biodiversity non-timber forest products; Oil solubility; NRTL model; Critical solution temperature;
Keywords: مدل NRTL; Deep eutectic solvents; Aqueous solutions; Molar enthalpies of mixing; Refractive indices; NRTL model;
Keywords: مدل NRTL; Vapor liquid equilibrium; Ionic liquids; Ethyl acetate; Ethanol; NRTL model; Ï-Profiles;
Keywords: مدل NRTL; Liquid-liquid equilibrium; Extraction; 5-Hydroxymethylfurfural; NRTL model;
Keywords: مدل NRTL; Aqueous biphasic systems; Binodal curves; Ionic liquids; Merchuk equation; Dipotassium hydrogen phosphate; NRTL model;
Keywords: مدل NRTL; l-asparagine monohydrate; Iso-propanol; Water; Solubility; UNIQUAC model; NRTL model; Solid-liquid equilibrium
Keywords: مدل NRTL; Aqueous biphasic systems; Phase diagram; Ionic liquids; Dipotassium carbonate; NRTL model
Keywords: مدل NRTL; (Liquid + liquid + solid) equilibrium; (Liquid + liquid) equilibrium; Temperature dependent Setschenow-type equation; NRTL model; Polyvinylpyrrolidone
Keywords: مدل NRTL; Molar excess enthalpy; Aqueous solutions; Alkanolamines and alkylamines; Redlich-Kister equation; NRTL model;
Keywords: مدل NRTL; Tars; Absorption model; Equilibrium stage; NRTL model; Soybean oil
Keywords: مدل NRTL; Vapor pressure; Ionic liquid; NRTL model; Extractive distillation
Keywords: مدل NRTL; Heavy oil; Bitumen characterization; Simulated distillation; Solubility; NRTL model;
Keywords: مدل NRTL; Vapor pressure; Ionic liquid; NRTL model; Extractive distillation
Keywords: مدل NRTL; (Liquid + liquid) equilibrium; Aromatics; Phosphoric acid; NRTL model; UNIQUAC model;
Keywords: مدل NRTL; Solubility; Water; Ionic liquid; NRTL model
Keywords: مدل NRTL; Separation factor; Phase equilibrium; Ionic liquid; NRTL model
Keywords: مدل NRTL; MD; Membrane distillation; VMD; Vacuum membrane distillation; TP; Tubular membrane module; CP; Capillary membrane module; NRTL model; Non-random to liquid model; PP; Polypropylen; Vacuum membrane distillation; Simulation user model; AspenPlus©; Activity
Keywords: مدل NRTL; Counter-current chromatography; Solvent system selection; NRTL model; Prediction of partition coefficient; Malus hupehensis
Keywords: مدل NRTL; Liquid–liquid equilibrium; Ionic liquids; NRTL model; Acetone; N-Butanol; Ethanol
Keywords: مدل NRTL; Butyric acid; LLE data; Ternary mixture; NRTL model; UNIQUAC model
Keywords: مدل NRTL; Vapor-liquid equilibrium; Peng-Robinson equation; NRTL model; UNIQUAC model; Binary interaction parameters; Particle swarm optimization; Ant colony optimization;
Keywords: مدل NRTL; Liquid-liquid equilibria; n-propyl propionate; NRTL model
Keywords: مدل NRTL; n-Alkane; Methyl myristate; VLE; NRTL model; UNIQUAC model; Wilson model
Keywords: مدل NRTL; [Bmim][NO3]; [Omim][NO3]; Ethyl benzene; p-xylene; Alkane; NRTL model
Keywords: مدل NRTL; Benzene; Heptane; [BPy][NO3]; [HPy][NO3]; NRTL model
Keywords: مدل NRTL; Vapor–liquid equilibrium; Ionic liquids; 2-Propanol; Water; NRTL model
Keywords: مدل NRTL; Vapor–liquid equilibrium; Ionic liquid; Methyl acetate; Methanol; NRTL model
Comment regarding the paper “Solubility determination and thermodynamic modelling of 3,5-dimethylpyrazole in nine organic solvents from Tâ¯=â¯(283.15 to 313.15)â¯K and mixing properties of solutions”
Keywords: مدل NRTL; 3,5-Dimethylpyrazole; Solubility; NRTL model;
Experimental result and data correlation of liquid-liquid equilibrium for methyl isopropyl ketoneâ¯+â¯o, m, p-dihydroxybenzeneâ¯+â¯water at 333.15â¯K, 343.15â¯K and 353.15â¯K
Keywords: مدل NRTL; Liquid-liquid equilibrium; MIPK; Dihydroxybenzene; NRTL model; UNIQUAC model;
Effect of bis(trifluoromethylsulfonyl)imide-based ionic liquids on the isobaric vapor - liquid equilibrium behavior of ethanol + dimethyl carbonate at 101.3 kPa
Keywords: مدل NRTL; Vapor - liquid equilibrium; Ethanol; DMC; Ionic liquids; NRTL model;
Isobaric vapor-liquid equilibrium for acetone + methanol system containing different ionic liquids at 101.3 kPa
Keywords: مدل NRTL; Vapor-liquid equilibrium; Ionic liquid; Acetone; Methanol; NRTL model;
Separation of acetonitrile + ethanol mixture using imidazolium - Based ionic liquids as entrainers
Keywords: مدل NRTL; Vapor-liquid equilibrium; Ionic liquids; Acetonitrile; Ethanol; NRTL model;
Separation of acetonitrile and methanol azeotropic mixture using imidazolium-based ionic liquids as entrainers
Keywords: مدل NRTL; Vapor-liquid equilibrium; Ionic liquids; Acetonitrile; Methanol; NRTL model; Ï-Profiles;
Isobaric vapor-liquid equilibrium for 2-butanone + ethanol + phosphate-based ionic liquids at 101.3 kPa
Keywords: مدل NRTL; Vapor liquid equilibrium; Ionic liquids; 2-Butanone; Ethanol; NRTL model;
Remarks and further analysis on “Solubility and dissolution thermodynamic properties of 1,6-Bis[3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionamido]hexane in pure solvents and binary solvent mixtures”
Keywords: مدل NRTL; Irganox 1098; Solubility; NRTL model; Preferential solvation;
Vapor-liquid equilibrium of 2,3,3,3-tetrafluoroprop-1-ene with 1-butyl-3-methylimidazolium hexafluorophosphate, 1-hexyl-3-methyl imidazolium hexafluorophosphate, and 1-octyl-3-methylimidazolium hexafluorophosphate
Keywords: مدل NRTL; R1234yf; Ionic liquids; Vapor-liquid phase equilibrium; NRTL model;
Measurement and correlation of isobaric binary vapor-liquid equilibria for water and 2-propanol each with 1-butyl-1-methypyrrolidinium chloride and 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate
Keywords: مدل NRTL; Vapor-liquid equilibrium; Ionic liquids; Pyrrolidinium ionic liquids; Water, 2-propanol; NRTL model;
Thermodynamic modeling studies of aqueous solubility of caffeine, gallic acid and their cocrystal in the temperature range of 303Â K-363Â K
Keywords: مدل NRTL; Caffeine; Gallic acid; Cocrystal; NRTL model; Predicting solubility; Molecular dynamic simulation;
The experimental investigations on viscosity, surface tension, interfacial tension and solubility of the binary and ternary systems for tributyl phosphate (TBP) extractant in various organic solvents with water: Thermodynamic NRTL model and molecular inte
Keywords: مدل NRTL; Viscosity; Surface tension; Interfacial tension; Solubility; TBP; NRTL model;
Liquid - liquid equilibrium for the quaternary reaction system water + sec-butyl alcohol + sec-butyl acetate + acetic acid
Keywords: مدل NRTL; LLE; Quaternary reaction system; Sec-butyl acetate; NRTL model; UNIQUAC model;
Binary and ternary solid-liquid phase equilibrium for the systems formed by succinic acid, urea and diethylene glycol: Determination and modelling
Keywords: مدل NRTL; Solid-liquid phase equilibrium; Phase diagram; Succinic acid; Urea; Diethylene glycol; NRTL model;
Measurements and correlation of liquid-liquid equilibrium data for the ternary (3-heptanone + phenol + water) system
Keywords: مدل NRTL; Phenol; LLE data; Correlation; NRTL model; UNIQUAC model; 3-Heptanone;
Liquid–liquid equilibrium extraction of ethanol with mixed solvent for bioethanol concentration
Keywords: مدل NRTL; Bioethanol; Solvent extraction; NRTL model
Liquid–liquid extraction of toluene from alkane with pyridinium based ionic liquid ([BPy][NO3] and [HPy][NO3]) at 298.15 K and atmospheric pressure
Keywords: مدل NRTL; [BPy][NO3]; [HPy][NO3]; Toluene; Alkane; NRTL model
Liquid-liquid equilibria for methyl isobutyl ketone + cresols + water at 333.15 K, 343.15 K and 353.15 K: Experimental results and data correlation
Keywords: مدل NRTL; Liquid-liquid equilibria; Cresol; Methyl isobutyl ketone; NRTL model; UNIQUAC model;
Phase equilibria of three binary systems containing 2,5-dimethylthiophene and 2-ethylthiophene in hydrocarbons
Keywords: مدل NRTL; Isobaric vapor–liquid equilibrium; 2-Ethylthiophene; 2,5-Dimethylthiophene; NRTL model; UNIFAC 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 NRTL; Vapor-liquid equilibrium; 2-Methylthiophene; Wilson model; NRTL model; Original UNIFAC model;
Liquid–liquid equilibria study of the (water + phosphoric acid + hexyl or cyclohexyl acetate) systems at T = (298.15, 308.15, and 318.15) K: Measurement and thermodynamic modelling
Keywords: مدل NRTL; Liquid–liquid equilibrium; Phosphoric acid; NRTL model; UNIQUAC model; LSER approach
Correlation and prediction of the solubility of the racemic tartaric acid-ethanol-water system with the NRTL model
Keywords: مدل NRTL; Racemic tartaric acid; Solid-liquid equilibria; Solubility-temperature dependence; Correlation; NRTL model;