1 - 6 |
Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates Verevkin SP, Toktonov AV, Chernyak Y, Schaffner B, Borner A |
7 - 13 |
Some useful expressions for deriving component fugacity coefficients from mixture fugacity coefficient Hu JW, Wang R, Mao SD |
14 - 20 |
Experimental and predicted phase equilibria and excess properties for systems with ionic liquids Liebert V, Nebig S, Gmehling J |
21 - 33 |
Experimental densities and derived thermodynamic properties of liquid propan-1-ol at temperatures from 298 to 423 K and at pressures up to 40 MPa Abdulagatov IM, Safarov JT, Aliyev FS, Talibov MA, Shahverdiyev AN, Hassel EP |
34 - 38 |
Excess molar enthalpies of ethyl acetoacetate plus (methanol, +ethanol, +1-propanol, and +2-propanol) at T = (298.15, 313.15 and 328.15) K and p = (0.1 and 10.0) MPa Gao H, Li SY, Yan WD |
39 - 44 |
Isothermal vapour-liquid equilibria of binary systems of 1,2-dichloroethane with ethers Amireche-Ziar F, Boukais-Belaribi G, Jakob A, Mokbel I, Belaribi FB |
45 - 50 |
Predicting phase diagram of the CaCl2 center dot H2O binary system from the BET adsorption isotherm Ally MR |
51 - 60 |
A similarity variable for estimating the heat capacity of solid organic compounds - Part I. Fundamentals Lastovka V, Sallamie N, Shaw JM |
61 - 67 |
Prediction of volumetric and thermodynamic properties of two aromatic-alcohol mixtures using GMA equation of state Goharshadi EK, Abareshi M |
68 - 73 |
Vapor-liquid equilibrium data for the (hexafluoroethane+1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353 K and pressures up to 4.16 MPa Madani H, Valtz A, Coquelet C, Meniai AH, Richon D |
74 - 84 |
Evaluation of COSMO-RS for the prediction of LLE and VLE of water and ionic liquids binary systems Freire MG, Ventura SPM, Santos LMNBF, Marrucho IM, Coutinho JAP |
85 - 89 |
Liquid-liquid equilibrium of substituted perfluoro-n-octane plus n-octane systems Varanda FR, Vega LF, Coutinho JAP, Marrucho IM |
90 - 94 |
Osmotic and activity coefficients of dilute aqueous solutions of the series Me4Ni to MeBu3NI at 298.15 K Blanco LH, Amado GE, Calvo JC |
95 - 99 |
Determination of microscopic interaction constants by X-ray reflectivity measurements Lehmkuhler F, Paulus M, Streit-Nierobisch S, Tolan M |
100 - 108 |
A new molecular model for fluids - Part I. Pure substances Ibrahim B |
109 - 113 |
Effect of temperature and concentration of H3O+ ions on the intrinsic viscosity of poly(ethylene oxide) in aqueous solutions Mehrdad A, Rostami MR |
114 - 120 |
Structure of two-dimensional hard-disk mixtures: Modified fundamental-measure theory Kim SC, Suh SH, Seong BS |
121 - 129 |
Solubility of carbon dioxide in aqueous solutions of 2-amino-2-hydroxymethyl-1,3-propanediol Le Tourneux D, Iliuta I, Iliuta MC, Fradette S, Larachi F |
130 - 133 |
Vapor-liquid equilibrium and excess Gibbs energies of some binary mixtures of acrylonitrile at 95.5 kPa Prasad TEV, Nath ANV, Prasad DHL |
134 - 141 |
A similarity variable for estimating the heat capacity of solid organic compounds - Part II. Application: Heat capacity calculation for ill-defined organic solids Lastovka V, Fulem M, Becerra M, Shaw JM |
142 - 152 |
Phase diagrams for liquid-liquid equilibrium of ternary poly(ethylene glycol) plus di-sodium tartrate aqueous system and vapor-liquid equilibrium of constituting binary aqueous systems at T = (298.15, 308.15, and 318.15) K - Experiment and correlation Zafarani-Moattar MT, Hamzehzadeh S, Hosseinzadeh S |
153 - 158 |
Molecular connectivity indices method for correlating and estimating solubility of fatty acids, alcohols, esters and triglycerides in supercritical carbon dioxide Li HR, Li SF |