الرئيسية › دليل الباحثين › Jacques José
Jacques José
الانتماء : Lyon 1 Université · Centre National de la Recherche Scientifique · Laboratoire des Multimatériaux et Interfaces
- 63منشورات (انتماء فرنسي)
- 223مجموع المنشورات
- 2928الاستشهادات
- 31مؤشر h
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إنشاء ملفي المجاني إضافة منشوراتيمجالات البحث
- Phase Equilibria and Thermodynamics
- Chemical Thermodynamics and Molecular Structure
- Thermodynamic properties of mixtures
- Chemical and Physical Properties in Aqueous Solutions
- Crystallization and Solubility Studies
المنشورات (63)
- Experimental vapor-liquid equilibria of pure compounds and binary systems (furfural + γ-valerolactone or γ-butyrolactone) and (5-methylfurfural + γ-valerolactone or γ-butyrolactone) encountered in biorefineries
- Experimental Vapor-Liquid Equilibria of Pure Compounds and Binary Systems (Furfural +Γ-Valerolactone or Γ-Butyrolactone) and (5-Methylfurfural + Γ-Valerolactone or Γ-Butyrolactone) Encountered in Biorefineries
- Experimental vapor-liquid equilibria of pure compounds and binary systems (furfural + γ-valerolactone or γ-butyrolactone) and (5-methylfurfural + γ-valerolactone or γ-butyrolactone) encountered in biorefineries
- Isothermal vapor–liquid equilibria of binary mixtures containing (methanol, or propan-1-ol, or water, or acetonitrile) and 1-ethyl-3-methylimidazolium thiocynate ionic liquid: Measurements and modeling
- Isothermal Vapor–Liquid Equilibria of Binary Mixtures Containing N,N-Dimethylacetamide with 1,3,5-Trimethylbenzene or Propan-2-ol or Dimethyl Sulfoxide
- Experimental and predicted aqueous solubility and vapor pressures of food packaging migrants: 4-n-octylphenol, 4-tert-octylphenol and 4-n-nonylphenol
- Isothermal vapor-liquid equilibria for binary liquid mixtures of ethylmercaptan and propylmercaptan with some common solvents
- Phase Equilibrium Properties of Binary Systems (Furfural + Ethanol or Butan-2-ol) at Several Temperatures
- Isothermal Vapor–Liquid Equilibria and Excess Gibbs Energy for Binary Liquid Mixtures of 1,2-Dichloroethane with Some Aliphatic Polyethers
- Experimental measurements for the liquid-liquid equilibrium of ternary systems [(water + methyl oleate + model mixtures of tar (naphthalene, phenanthrene and anthracene)] issued from the biomass gasification process
- Vapor–Liquid Equilibria, Density, Sound Velocity, and Refractive Index for Binary Mixtures Containing 2-(2-Ethoxyethoxy)ethanol and 1-Propanol or 2-Propanol or 1-Butanol or 2-Butanol at Different Temperatures
- Recovery of Butanol from a Bioreactor. Phase Equilibria for Extracting Butanol from a Dilute Aqueous Solution Using Dodecane or 1,3,5-Trimethylbenzene
- Excess molar enthalpies of dimethyl sulfoxide or sulfolane with aliphatic/aromatic hydrocarbons
- Experimental solubility of carbon dioxide in monoethanolamine, or diethanolamine or N-methyldiethanolamine (30 wt%) dissolved in deep eutectic solvent (choline chloride and ethylene glycol solution)
- Experimental Measurements and Modeling Study of Liquid–Liquid Equilibrium [(Water + Methyl Oleate + Model Molecules of Tar Issued from the Biomass Gasification Process (Benzene, Toluene, Phenol, Thiophene, and Pyridine)]
- Vapour-liquid equilibria, enthalpy of vaporisation, and excess Gibbs energies of binary mixtures of {3,3-diamino-N-methyldipropylamine (DNM) (or N,N,N′,N′′,N′′-pentamethyldiethylenetriamine (PMDETA)) + water}
- Isothermal Vapor–Liquid Equilibria and Excess Gibbs Energies for Binary Mixtures of Cyclic Ethers with 1,2-Dichloroethane
- CO 2 Capture Using Deep Eutectic Solvent and Amine (MEA) Solution
- Phase equilibrium measurements and thermodynamic modeling of binary mixtures containing a diesel compound n-dodecane + biodiesel compounds: Ethyl dodecanoate and ethyl octanoate
- Vapor-liquid equilibria, density and sound velocity measurements of (water or methanol or ethanol + 1,3-propanediol) binary systems at different temperatures
- Phase equilibrium properties of binary mixtures containing a diesel compound (n-dodecane) + biodiesel compounds (ethyl hexanoate, ethyl decanoate and ethyl tetradecanoate)
- Liquid–vapor equilibria of pure and aqueous solutions of diethylenetriamine or dipropylenetriamine
- Phase equilibrium measurements and thermodynamic modeling of aqueous solutions of polyamines CO2 absorbents: 3-aminopropylmethylamine, 3-aminopropyldimethylamine and N,N-diethyl 1,3-propanediamine at temperatures from 273 K to 363 K
- Isothermal vapor–liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
- Corrigendum to “Measurement and correlation of vapour pressures of pyridine and thiophene with [EMIM][SCN] ionic liquid” [J. Chem. Thermodyn. 72 (2014) 134–138]
- Corrigendum to “Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures” [J. Chem. Thermodyn. 54 (2012) 83–89]
- Measurement and correlation of vapour pressures of pyridine and thiophene with [EMIM][SCN] ionic liquid
- Vapor–liquid equilibria of N,N,N′,N′ tetramethylethylenediamine (TMEDA), tetramethylpropylenediamine (TMPDA) and their aqueous solutions
- Phase equilibrium properties of binary mixtures containing 1,3-pentanediamine (or 1,5-diamino-2-methylpentane) and water at several temperatures
- Isothermal vapour pressures and thermodynamic excess properties of 3,5- and 2,6-dimethylpyridine with cyclohexane. Measurements and prediction
- Solubility of carbon dioxide gas in some 2.5M tertiary amine aqueous solutions
- Isothermal Vapor–Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
- Thermodynamic excess properties of 3,5- and 2,6-dimethylpyridine with cyclohexane measurement and prediction
- Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
- Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
- Liquid–vapor equilibria of binary systems containing alcohols (1-butanol, or 2-butanol or 1-hexanol) present in the production by chemical process of 2,5-dimethyl furan from biomass
- Experimental determination of the isothermal (vapour + liquid) equilibria of binary aqueous solutions of sec-butylamine and cyclohexylamine at several temperatures
- Phase equilibrium properties of binary aqueous solutions containing ethanediamine, 1,2-diaminopropane, 1,3-diaminopropane, or 1,4-diaminobutane at several temperatures
- Phase equilibrium properties of binary aqueous solutions of benzylamine, 1,2-bis(2-aminoethoxy)ethane, or 2-[2-(dimethylamino)ethoxy]ethanol
- Isothermal vapor–liquid equilibria and excess enthalpies of binary mixtures of propyl ethanoate+1-hexyne, +2-hexyne, +3-hexyne
- Isothermal Vapor−Liquid Equilibria of (Monoethanolamine + Water) and (4-Methylmorpholine + Water) Binary Systems at Several Temperatures
- Isothermal Vapor−Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
- Excess properties and vapour pressure of (3-diethylaminopropylamine +n-alkanes)
- Vapour–liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether ‘DIPE’ and monoaromatic hydrocarbons
- Isothermal vapour–liquid equilibria and excess molar enthalpies of hex-2-yne+methyl butyl ether and hex-3-yne+dibutyl ether mixtures
- Isothermal Vapor−Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
- Thermodynamics of isomeric hexynes+MTBE binary mixtures
- Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
- Vapour pressures and excess functions of (3,5; 2,6)dimethylpyridine+n-hexane, n-heptane and n-octane measurement and prediction
- Excess volume, excess enthalpy and vapour–liquid equilibria of N,N,N′,N′-tetramethyl-1,3-butanediamine + n-heptane or + cyclohexane mixtures
- Thermodynamics of n-octane+hexynes binary mixtures
- Equilibres Liquide-vapeur Isothermes De Melanges Binaires, Amine+amine
- Influence of the Pressure and Temperature on the Viscosity and Density of Binary Water + DAA
- Vapour pressures and excess functions of N, N, N′, N′-tetramethylalkanediamine + cyclohexane. A group contribution study of the NN proximity effect
- Vapour pressures and excess functions of 1,4-dimethylpiperazine + n-heptane, or cyclohexane measurement and prediction
- Excess properties of N,N,N′,N′-tetramethylalkanediamine + n-heptane: A study of the N-N proximity effect
- Equilibres liquide-vapeur isothermes de melanges binaires de la piperidine et de la N-methyl piperidine avec certains ethers
- Solid-liquid phase equilibria for diethylamine or triethylamine + n-alkanes
- Equilibres liquide-vapeur isothermes de melanges binaires formes de composes heterocycliques tels que: Morpholine, tetrahydropyranne, piperidine et 1,4-dioxane
- Equilibres liquide-vapeur isothermes de melanges binaires de la piperidine et de la N-methyl piperidine avec certains ethers
- Solid-liquid phase equilibria for tetrachloromethane + n-alkanes
- Diagramme d’equilibre liquide-solide de systemes binaires pyridine+n-alcanes
- Isothermal vapor-liquid equilibria for the 2-butanone + benzene + n-octane system
المؤلفون المشاركون
- Ilham Mokbel
- Latifa Négadi
- Christelle Goutaudier
- Fatiha Dergal
- Fabrice Mutelet
- Najet Yagoubi
- Ahmed Ait-Kaci
- Mohammed-Ridha Mahi
- Aouicha Belabbaci
- Oussama Khelidj
- Ibtissem Guennoun
- Jürgen Gmehling
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