1 - 21 |
Distribution of hydrochloric, nitric, and sulfuric acids between water and organic solutions of tri-n-octylamine - Part I. Toluene as organic solvent Schunk A, Maurer G |
23 - 34 |
Solubility of H2S in (H2O plus piperazine) and in (H2O plus MDEA plus piperazine) Xia JZ, Kamps APS, Maurer G |
35 - 52 |
Determination of the accuracy of truncated Leiden and Berlin virial expansions for pure gases Eubank PT, Kruggel-Emden H, Santana-Rodriguez G, Wang XN |
53 - 67 |
Vapor-liquid equilibrium data for the CO2+1, 1,1,2,3,3,3,-heptafluoropropane (R227ea) system at temperatures from 276.01 to 367.30 K and pressures up to 7.4 MPa Valtz A, Coquelet C, Baba-Ahmed A, Richon D |
69 - 80 |
Development of a modified Bromley methodology for the estimation of ionic media effects on solution equilibria - Part 6. The chemical model of phosphoric acid in aqueous solution at 25 degrees C and comparison with arsenic acid Raposo JC, Zuloaga O, Olazabal MA, Madariaga JM |
81 - 95 |
Development of a Modified Bromley Methodology for the estimation of ionic media effects on solution equilibria - Part 5. The chemical model of boric acid in aqueous solution at 25 degrees C and comparison with arsenious acid Raposo JC, Zuloaga O, Olazabal MA, Madariaga JM |
97 - 109 |
Vapour pressures at 10 different temperatures between 278.15 and 323.15 K for binary mixtures of 1-bromobutane with ethanol or 1-hexanol Garriga R, Martinez S, Perez P, Gracia M |
111 - 130 |
An equation of state and compressed liquid and supercritical densities for sulfur dioxide Ihmels EC, Lemmon EW, Gmehling R |
131 - 142 |
Experimental determination of carbon dioxide and nitrous oxide co-solubility in liquid oxygen De Stefani V, Baba-Ahmed A, Richon D |
143 - 154 |
Experimental study on the solubility of natural gas components in water with or without hydrate inhibitor Wang LK, Chen GJ, Han GH, Guo XQ, Guo TM |
155 - 165 |
Effect of salt and volume ratio on the reverse micellar extraction of lysozyme using DODMAC Shin YO, Weber ME, Vera JH |
167 - 181 |
Equation of state for square-well fluids: development of a coordination number model Nasrifar K, Jalali F |
183 - 192 |
Solubility of solid solutes in supercritical carbon dioxide with and without cosolvents Li QS, Zhang ZT, Zhong CL, Liu YC, Zhou QR |
193 - 207 |
Excess molar volume and viscosity study for the ternary system tetrahydrofuran (1)+1-chlorobutane (2)+1-butanol (3) at 283.15, 298.15 and 313.15 K Postigo M, Mariano A, Mussari L, Camacho A, Urieta J |
209 - 223 |
Viscosity B-coefficients and activation parameters for viscous flow of the solution of hexanedioic acid in water plus poly(ethylene glycol) mixed solvents at 298.15-313.15 K Bai TC, Huang CG, Li Q |
225 - 246 |
Modelling of the surface tension of pure components with the gradient theory of fluid interfaces: a simple and accurate expression for the influence parameters Miqueu C, Mendiboure B, Graciaa A, Lachaise J |
247 - 261 |
Solvent activities of ordinary and associated binary polymer solutions: group-contribution method Chang BH, Bae YC |
263 - 281 |
Prediction of vapor pressures of solid organic compounds with a group-contribution method Coutsikos P, Voutsas E, Magoulas K, Tassios DP |
283 - 300 |
Volumetric and thermodynamic properties for pure refrigerants and refrigerant mixtures from cubic equations of state Feroiu V, Geana D |
301 - 317 |
Non-ideality of methanol solution's of artificial serum in the mole fraction range from 5 x 10(-4) to 5 x 10(-3) at 25 degrees C Ralloff KPG, Westh P, Purssell RA, Pudek M, Koga Y |
319 - 321 |
Comments on a publication by J. Garcia-Gonzalez, M.J. Molina, F. Rodriguez, R Mirada, "Solubilities of hydroquinone and p-quinone in supercritical carbon dioxide" [Fluid Phase Equilib. 200(2002)31-39] Deiters UK |