1 - 21 |
Surface and interfacial tensions of the systems water plus n-butyl acetate plus methanol and water plus n-pentyl acetate plus methanol at 303.15 K Santos BMS, Ferreira AGM, Fonseca IMA |
23 - 51 |
Thermodynamic and IR spectroscopic studies of solutions with simultaneous association and solvation Asprion N, Hasse H, Maurer G |
53 - 68 |
Measurements and modeling of high-pressure phase behavior of binary CO2-amides systems Byun HS, Kim NH, Kwak C |
69 - 81 |
Excess enthalpies of the ternary mixtures: diisopropyl ether plus (2,2,4-trimethylpentane or n-heptane) plus methylcyclohexane at 298.15 K Wang ZH, Benson GC, Lu BCY |
83 - 89 |
Ultrasonic studies of some derivatives of 6-ethylbenzene-1,3-diol in 1,4-dioxane Baluja S, Oza S |
91 - 98 |
Thermodynamic interactions of 2,3-butanediol with water Kapadi UR, Hundiwale DG, Patil NB |
99 - 113 |
Enhanced density-based models for solid compound solubilities in supercritical carbon dioxide with cosolvents Sauceau M, Letourneau JJ, Richon D, Fages J |
115 - 121 |
Vapor-liquid equilibria for the binary system hexan-1-ol plus tert-butyl methyl ether (MTBE) at 298.15, 318.15, and 338.15 K de Llano JJ, Segade L, Jimenez E, del Rio A, Renuncio JAR, Pando C |
123 - 139 |
Vapour-liquid coexistence properties and critical points of two branched alkanes series Wescott JT, Kung P, Nath SK |
141 - 154 |
Automated measuring device of (p, rho, T) data - Application to the 1-hexanol plus n-hexane system Troncoso J, Bessieres D, Cerdeirina CA, Carballo E, Romani L |
155 - 169 |
Vapor-liquid equilibria of the binary mixtures nitrogen plus methane, nitrogen plus ethane and nitrogen plus carbon dioxide, and the ternary mixture nitrogen plus methane plus ethane from Gibbs-ensemble molecular simulation Carrero-Mantilla J, Llano-Restrepo M |
171 - 188 |
Thermal diffusion sensitivity to the molecular parameters of a binary equimolar mixture, a non-equilibrium molecular dynamics approach Galliero G, Duguay B, Caltagirone JP, Montel F |
189 - 198 |
Theory of melting point depression for SPE/salt systems; applicability of the extended PHSC model Ko SJ, Bae YC |
199 - 221 |
Critical curves of liquid-liquid equilibria in ternary systems - Description by a regular-solution model Novak JP, Rehak K, Vonka P, Matous J |
223 - 238 |
Henry's constants of butane, isobutane, 1-butene and isobutene in methanol at 255-320 K Miyano Y, Nakanishi K, Fukuchi K |
239 - 245 |
Solubilities of carbon dioxide in aqueous solutions of triisopropanolamine Chauhan RK, Yoon SJ, Lee H, Yoon JH, Shim JG, Song GC, Eum HM |
247 - 260 |
Crystallisation of heavy hydrocarbons from three synthetic condensate gases at high pressure Jensen MR, Ungerer P, de Weert B, Behar E |
261 - 263 |
About "Studies of viscosity and excess molar volume of binary mixtures of propane-1,2 diol with water at various temperatures" by U.R. Kapadi, D.G. Hundiwale, N.B. Patil, M.K. Lande, P.R. Patil [Fluid Phase Equilib. 192 (2001) 63-70] Linek J |
265 - 290 |
Solubility of CO2 in water from -1.5 to 100 degrees C and from 0.1 to 100 MPa: evaluation of literature data and thermodynamic modelling Diamond LW, Akinfiev NN |
291 - 301 |
Verifying reciprocal relations for experimental diffusion coefficients in multicomponent mixtures Medvedev OO, Shapiro AA |
303 - 313 |
Vapour-liquid equilibrium compositional data for a model fluid at elevated temperatures and pressures Gozalpour F, Danesh A, Todd AC, Tohidi B |