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The Journal of Chemical Thermodynamics, ISSN 0021-9614, 07/2017, Volume 110, pp. 243 - 251
[Display omitted] •Solubility for quaternary system of adipic acid+succinic acid+glutaric acid+ethanol were determined.•The quaternary phase diagrams were... 
Succinic acid | Solid-liquid phase equilibrium | Ethanol | Adipic acid | Phase diagram | Glutaric acid | THERMODYNAMIC PROPERTIES | CHEMISTRY, PHYSICAL | TERNARY-SYSTEM | SOLUBILITY | MIXTURES | DICARBOXYLIC-ACIDS | THERMODYNAMICS | ORGANIC-SOLVENTS | CYCLOHEXANONE | 318.15 K | Alcohol | Alcohol, Denatured | Analysis
Journal Article
Fluid Phase Equilibria, ISSN 0378-3812, 02/2016, Volume 409, pp. 256 - 263
In this work, the solid–liquid phase equilibrium data for ternary system of adipic acid + glutaric acid + ethanol were measured using an isothermal saturation... 
Solid–liquid phase equilibrium | Ethanol | Adipic acid | Phase diagram | Glutaric acid | Solid-liquid phase equilibrium | Alcohol | Alcohol, Denatured | Analysis | Thermodynamics | Phase diagrams | Correlation | Ternary systems | Solubility | Ethyl alcohol | Mathematical models
Journal Article
The Journal of Chemical Thermodynamics, ISSN 0021-9614, 04/2017, Volume 107, pp. 8 - 17
[Display omitted] •SLE for ternary system of succinic acid+glutaric acid+ethanol was determined.•The ternary phase diagrams were constructed at 283.15K,... 
Succinic acid | Solid-liquid phase equilibrium | Ethanol | Phase diagram | Glutaric acid | Alcohol | Alcohol, Denatured | Analysis
Journal Article
Journal of Molecular Liquids, ISSN 0167-7322, 05/2017, Volume 234, pp. 164 - 171
In this work, the solid-liquid phase equilibrium data for ternary system of 4-nitrobenzaldehyde+3-nitrobenzaldehyde+ethyl acetate were determined by using an... 
Solid-liquid phase equilibrium | Thermodynamic model | Phase diagram | Nitrobenzaldehyde | Thermodynamics | Esters | Models | Analysis
Journal Article
Journal of Chemical & Engineering Data, ISSN 0021-9568, 06/2016, Volume 61, Issue 6, pp. 2105 - 2113
The solid–liquid phase equilibrium for the ternary succinic acid + adipic acid + ethanol system was determined at 283.15, 303.15, and 313.15 K, respectively,... 
Journal Article
Fluid Phase Equilibria, ISSN 0378-3812, 06/2016, Volume 417, pp. 242 - 247
The solid–liquid equilibrium (SLE) for ternary system of caprolactam + cyclohexanone oxime + methyl tert-butyl ether were determined at three temperatures of... 
Caprolactam | Methyl tert-butyl ether | Solid-liquid equilibrium | Cyclohexanone oxime | Phase diagram | Oximes | Phase diagrams | Cyclohexanone | Ternary systems | Crystallization | Phase equilibria | Ethers
Journal Article
The Journal of Chemical Thermodynamics, ISSN 0021-9614, 04/2018, Volume 119, pp. 76 - 83
[Display omitted] •Low viscosity [Hmim][NTf2] ionic liquid was used in the extraction of phenol from water.•The equilibrium data were obtained using the cloud... 
Separation factor | LLE correlation | Phenol | Experimental LLE | Ionic liquid | AQUEOUS-SOLUTIONS | PARTITION-COEFFICIENTS | AB-INITIO CALCULATIONS | CHEMISTRY, PHYSICAL | IMIDAZOLIUM | TERNARY-SYSTEM | PRESSURE | EXTRACTION | THERMODYNAMICS | 1-HEXYL-3-METHYLIMIDAZOLIUM BIS(TRIFLUOROMETHYLSULFONYL)IMIDE | ORGANIC-SOLVENTS | ALKYL CHAIN-LENGTH
Journal Article
The Journal of Chemical Thermodynamics, ISSN 0021-9614, 10/2017, Volume 113, pp. 257 - 262
•The vapour liquid and vapour liquid liquid phase equilibrium for (R717+R1234yf) at temperatures from 243.150 to 283.150K were measured.•The volumetric... 
Azeotropic refrigerant | Ammonia | 2,3,3,3-Tetrafluoroprop-1-ene | (Vapour + liquid) equilibrium | (Vapour + liquid) equilibrium | PRESSURE | EQUATION-OF-STATE | THERMODYNAMICS | AMMONIA | R1234YF | CHEMISTRY, PHYSICAL | (Vapour plus liquid) equilibrium Ammonia | REFRIGERATION | Analysis | Global warming
Journal Article
Fluid Phase Equilibria, ISSN 0378-3812, 09/2017, Volume 448, pp. 143 - 151
Deep eutectic solvents (DES) are a new type of solvents that share some characteristics with Ionic Liquids while being cheaper, easier to prepare and, in some... 
Gallic acid partition | Hydrogen bonds | Thermogravimetric analysis | Quaternary systems | Deep eutectic solvents | EXTRACTION MEDIA | MOLECULAR-WEIGHT | CHEMISTRY, PHYSICAL | SALTS | ENGINEERING, CHEMICAL | THERMODYNAMICS | PHASE-BEHAVIOR | EQUILIBRIUM | PROTEIN SEPARATION | BIPHASIC SYSTEMS | IONIC LIQUIDS | POLYETHYLENE-GLYCOL | TETRAFLUOROBORATE
Journal Article
Fluid Phase Equilibria, ISSN 0378-3812, 08/2016, Volume 421, pp. 93 - 103
The partitioning behavior of the perchlorate ion on the aqueous two phase system (ATPS) NaNO3 + poly(ethylene glycol) 4000 (PEG 4000) + H2O was studied at... 
Partition | poly(ethylene glycol) | Aqueous two-phase system | Perchlorate ion | Poly(ethylene glycol) | EXCESS GIBBS ENERGY | BEHAVIOR | CHEMISTRY, PHYSICAL | COPOLYMERS | GLYCOL | HYDRATION | DENSITY | ENGINEERING, CHEMICAL | EXTRACTION | THERMODYNAMICS | EQUILIBRIUM | BIPHASIC SYSTEMS | Partitions | Correlation | Mathematical models | Nanostructure | Glycols | Perchlorates | Coefficients | Concentration gradient
Journal Article
Fluid Phase Equilibria, ISSN 0378-3812, 10/2014, Volume 379, pp. 185 - 190
Phase equilibrium (LLE) data of the solubility (binodal) curves and tie-line end compositions were examined for mixtures of {(water (1)+butyric acid+butyl... 
Butyl acetate | UNIQUAC | NRTL | LLE | Butyric acid | AQUEOUS-SOLUTIONS | TOLUENE | CHEMISTRY, PHYSICAL | GLUTARATE | ENGINEERING, CHEMICAL | DIETHYL SUCCINATE | THERMODYNAMICS | LIQUID-LIQUID EQUILIBRIA | EXTRACTION EQUILIBRIA | Saturated fatty acids | Analysis | Correlation | Mathematical analysis | Ternary systems | Solubility | Consistency | Phase equilibria | Mathematical models | Acetates
Journal Article
The Journal of Chemical Thermodynamics, ISSN 0021-9614, 12/2017, Volume 115, pp. 19 - 26
•Isobaric VLE data of the systems TFP+water/chloroform/p-xylene were measured at 101.3kPa.•The thermodynamic consistency of the VLE data was checked by four... 
Azeotropic distillation | Chloroform | p-Xylene | 2,2,3,3-Tetrafluoro-1-propanol | Vapour-liquid equilibrium | BENZENE | ACID | BINARY-SYSTEMS | ISOBUTYL ACETATE | CHEMISTRY, PHYSICAL | THERMODYNAMIC EXCESS FUNCTIONS | MIXTURES | THERMODYNAMICS | VAPOR-LIQUID-EQUILIBRIUM | 101.33 KPA | FLUORINATED ALCOHOLS | WATER | Paraxylene | Thermodynamics | Analysis
Journal Article
The Journal of Chemical Thermodynamics, ISSN 0021-9614, 07/2016, Volume 98, pp. 288 - 297
[Display omitted] •Solubility of 3,5-dichloroaniline in seven organic solvents were determined.•Solid–liquid phase equilibrium for ternary system was... 
3,5-Dichloroaniline | Solid–liquid phase equilibrium | 1,3,5-Trichlorobenzene | Phase diagram | Toluene | Solid-liquid phase equilibrium | Chlorobenzene | Thermodynamics | Models | Solvents | Ternary systems | Solubility | Phase equilibria | Ethyl acetate | Mathematical models | Acetone
Journal Article
Journal Article
Fluid Phase Equilibria, ISSN 0378-3812, 03/2016, Volume 412, pp. 1 - 8
Solid–liquid phase equilibrium data for binary (adipic acid + diethylene glycol) and (urea + diethylene glycol) systems at temperatures from (298.15–333.15) K... 
Urea | Diethylene glycol | Solid-liquid phase equilibrium | Adipic acid | Phase diagram | PLUS WATER | CHEMISTRY, PHYSICAL | 303.15 K | PARAMETERS | SOLUBILITY | MIXTURES | ENGINEERING, CHEMICAL | THERMODYNAMICS | SOLVENTS | TEMPERATURE | ETHANOL | SUCCINIC ACID | DIAGRAM | Glycols | Models | Analysis | Correlation | Interaction parameters | Ternary systems | Solubility | Ureas | Binary systems (materials)
Journal Article
Fluid Phase Equilibria, ISSN 0378-3812, 06/2016, Volume 417, pp. 96 - 108
We modified the binary interaction parameter in Wong-Sandler mixing rule for cubic EOS as a two-parameter linear function of composition. We then incorporated... 
CO2–CH4–H2O | Flash calculation | Non-random-two-liquid model | CO2–H2O | Wong-Sandler mixing rule | CH | Data points | Equations of state | Interaction parameters | Phase boundaries | Mathematical models | Modelling | Mixing rules | Binary systems (materials)
Journal Article