Keywords: CAPEX; capital expenditure; CED; conventional extractive distillation; CW; cooling water; CWP; cooling water pump; CWR; cooling water return; CWT; cooling water tower; ECI; eco-efficiency comparison index; EIED; energetically integrated extractive distill
مقالات ISI (ترجمه نشده)
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Keywords: Gas hydrate; Predictive model; Modified Huron-Vidal mixing rule; UNIQUAC; Phase equilibrium;
Keywords: Lattice theory; UNIQUAC; GEQUAC; COSMOSPACE; UNIFAC; COSMO-RS; COSMOSAC;
Keywords: Biofuel; Biodiesel; Supercritical methanol; Techno-economic; Low methanol to oil molar ratio; Economic analysis; SCA; supercritical alcohol; SCM; supercritical methanol; L-SCM; low methanol: oil molar ratio; Alkali-cat; homogeneous alkali-catalyzed proces
Keywords: Extractive distillation; Thermodynamic parameters; Phase behavior; UNIQUAC; TAC;
Keywords: Solid-liquid equilibrium; Long-chain aliphatic alcohol; Van Laar; Margules; NRTL; UNIQUAC;
Keywords: Flash point; Binary mixture; Wilson; NRTL; UNIQUAC; UNIFAC; UNIFAC-LBY; UNIFAC-DMD; UNIFAC-NIST;
Keywords: Valeric biofuels; Liquid-liquid equilibrium; NRTL; UNIFAC; UNIQUAC;
Keywords: Solubility; Sorbitol; Xylitol; Jouyban-Acree; NRTL; UNIQUAC;
Keywords: Extraction; Liquid-liquid equilibrium; Ionic liquids; Pyridine; NRTL; UNIQUAC;
Keywords: Liquid-liquid equilibrium; Cresols; Methyl isopropyl ketone; NRTL; UNIQUAC;
Keywords: Reactive phase equilibria; Modeling; Torrefaction; Volatile matter; UNIQUAC
Keywords: Lithium; Cathode; Equilibrium potential; NRTL; UNIQUAC;
Keywords: Liquid–liquid equilibria; Aromatic/decane separation; Ionic liquid; NRTL; UNIQUAC
Keywords: (Vapor + liquid) equilibria; Diamines; Water; NRTL; UNIQUAC; Modified UNIFAC (Do)
Keywords: Solubility; Polymorph; Measurement; Prediction; NRTL; UNIQUAC;
Keywords: Extractive distillation; Azeotropic mixtures; Simulation; Separation; UNIQUAC; Vapor-liquid equilibrium;
Keywords: ACM; Aspen Custom Modeler®; DMC; dimethyl carbonate; EA; evolutionary algorithm; MA; memetic algorithm; MC; main column; MeOH; methanol; MINLP; mixed-integer nonlinear programming; PF; penalty function; PFC; prefractionating column; PC; propylene carbona
Keywords: Vapor–liquid equilibria; Excess enthalpies; UNIQUAC; Separation factor
Keywords: Liquid–liquid equilibria; Butyric acid; Solvent; Ternary diagram; UNIQUAC; UNIFAC
Keywords: Wax; High pressure thermodynamic model; Solid-liquid phase equilibrium; UNIQUAC; Clapeyron;
Keywords: Adsorption; Isotherm; Vacancy solution; Wilson; NRTL; UNIQUAC; RVST;
Keywords: AA; acrylic acid; AP; Aspen Plusâ¢; BA; n-butyl acrylate; BuOH; n-butanol; FC; flow controller; HETP; height equivalent to a theoretical plate; HOC; Hayden O'Connell equation of state; IMP; impurity; LC; level controller; MV; middle vessel; RR; reflux
Keywords: Liquid-liquid equilibrium; Hexane; Ethyl acetate; NRTL; UNIQUAC; UNIFAC;
Keywords: LLE; n-hexane; Ethyl acetate; Acetonitrile; NRTL; UNIQUAC
Keywords: Flash point; Binary interaction parameters; Wilson; NRTL; UNIQUAC; NRTL-NRF
Keywords: Type 3 ternary; LLLE; Tie-triangle; Gibbs energy minimization; NRTL; UNIQUAC
Keywords: (Liquid + liquid) equilibrium; Sulfolane; n-Heptane; Carboxylic acid; NRTL; UNIQUAC
Keywords: Liquid–liquid equilibrium; 2-Propanol; Ionic liquids; NRTL; UNIQUAC
Keywords: Liquid-liquid equilibrium; Phase diagram; Selectivity; Glycerol; NRTL; UNIQUAC
Keywords: Vapor–liquid equilibria; Diethylenetriamine; Dipropylenetriamine; Enthalpy of vaporization; NRTL; UNIQUAC; Aqueous solutions of amine
Keywords: Activity coefficient models; Wilson; NRTL; UNIQUAC; Interaction parameters
Keywords: Wax precipitation; UNIQUAC; PC-SAFT; Petroleum fluids
Vapour-liquid equilibria, enthalpy of vaporisation, and excess Gibbs energies of binary mixtures of {3,3-diamino-N-methyldipropylamine (DNM) (or N,N,Nâ²,Nâ²â²,Nâ²â²-pentamethyldiethylenetriamine (PMDETA))â¯+â¯water}
Keywords: Vapour-liquid equilibria; Triamines; Enthalpy of vaporisation; NRTL; UNIQUAC;
Ternary liquid-liquid equilibrium of an azeotropic mixture (hexane + methanol) with different imidazolium-based ionic liquids at T = 298.15 K and 101.325 kPa
Keywords: LLE; ILs; Hexane; Methanol; NRTL; UNIQUAC;
Measurement and correlation of aqueous biphasic systems composed of alcohol (1-propanol/2-propanol/tert-butanol) + (NH4)2SO4 + H2O at 298â¯K and a textile dye partition
Keywords: Liquid-liquid equilibrium; NRTL; UNIQUAC; Textile dye extraction; Remazol Brilliant Blue R;
Quaternary and ternary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether)â¯+â¯furfuralâ¯+â¯acetic acidâ¯+â¯water between 298 and 343â¯K
Keywords: Liquid-liquid equilibria; Furfural; 2-Methyltetrahydrofuran; Cyclopentyl methyl ether; Acetic acid; UNIQUAC;
Ternary liquid-liquid equilibria for systems containing (dimethyl carbonate or methyl acetateâ¯+â¯methanolâ¯+â¯1-methylmidazole hydrogen sulfate) at 298.15â¯K and 318.15â¯K
Keywords: Liquid-liquid equilibria; Ionic liquid; Methanol; NRTL; UNIQUAC;
Liquid-liquid equilibria for the ternary system of waterâ¯+â¯furfuralâ¯+â¯solvents at 303.15 and 323.15â¯K under atmospheric pressure
Keywords: Liquid-liquid equilibria; Furfural; Water; Xylene; NRTL; UNIQUAC;
Thermodynamic properties of aqueous ternary system CuSO4â¯+â¯PEG 4000â¯+â¯H2O at different temperatures
Keywords: Water activity; Poly(ethylene glycol); Copper sulphate; UNIQUAC;
Experimental and modelling studies of pervaporative removal of odorous diacetyl and S-methylthiobutanoate from aqueous solutions using PEBA membrane
Keywords: Pervaporation; PEBA membrane; S-methylthiobutanoate and diacetyl; Mass transfer model; Feed concentration; PEBA; polyether block amide; PDMS; polydimethylsiloxane; PU; polyurethane; PC; polycarbonate; UNIQUAC; universal quasi-chemical; HB; hydrogen bond;
Thermodynamic modeling of the solvent extraction equilibrium for the recovery of vanadium (V) from acidic sulfate solutions using Di-(2-ethylhexyl) phosphoric acid
Keywords: Solvent extraction; Vanadium; D2EHPA; Thermodynamic modeling; Electrolyte UNIQUAC-NRF; UNIQUAC;
Modeling vapor-liquid equilibria of mixtures of SO2 and deep eutectic solvents using the CPA-NRTL and CPA-UNIQUAC models
Keywords: DES; Sulfur dioxide; Solubility; Thermodynamic modeling; UNIQUAC; NRTL;
Liquid-liquid extraction, COSMO-SAC predictions and process flow sheeting of 1-butanol enhancement using mesitylene and oleyl alcohol
Keywords: Mesitylene; Oleyl alcohol; NRTL; UNIQUAC; COSMO-SAC; 1-butanol; Aspen Plus;
Experimental measurement and thermodynamic modelling of liquid-liquid equilibria for the separation of 1,2-dichloroethane from cyclohexane using various extractants
Keywords: LLE; Cyclohexane; 1,2-dichloroethane; UNIQUAC; NRTL;
Liquid-liquid equilibrium of the ternary system water + propargyl alcohol + n-propyl acetate
Keywords: Liquid-liquid equilibrium; Propargyl alcohol; n-propyl acetate; UNIQUAC; NRTL;
Experiments and thermodynamic models for ternary liquid-liquid equilibrium systems of diethoxymethane + ethanol + water system at different temperatures
Keywords: Liquid-liquid equilibria; Diethoxymethane; Ethanol; Water; NRTL; UNIQUAC;
Measurement and thermodynamic modeling of ternary (liquid + liquid) equilibrium for extraction of ethanol from diethoxymethane solution with different solvents
Keywords: Liquid-liquid equilibria; Diethoxymethane; Ethanol; NRTL; UNIQUAC;
Application of 1-hexyl-3-methylimidazolium trifluoromethanesulfonate to the removal of alcohol from mixtures with heptane
Keywords: Liquid-liquid equilibrium; Alcohol; [Hmim][OTf]; NRTL; UNIQUAC; UNIFAC;
Liquid-liquid Equilibria (LLE) of the quaternary mixture (acetic acid + ethanol + ethyl acetate + water) arising out of esterification reaction: Optimization studies
Keywords: Propionic acid; Ethanol; Dowex 50Wx8-400; UNIQUAC; NRTL; RSM;