1 - 8 |
Effect of combining rules for cubic equations of state on the prediction of double retrograde vaporization Alfradique MF, Castier M |
9 - 14 |
Thermodynamic equations for a confined fluid at nanometric scale Meyra AG, Zarragoicoechea GJ, Kuz VA |
15 - 20 |
An improved method to predict second cross virial coefficients Vetere A |
21 - 28 |
Vapour-liquid equilibrium for the ethyl ethanoate+1-butene, +cis-2-butene, +trans-2-butene,+2-methylpropene, plus n-butane and+2-methylpropane Haimi P, Uusi-Kyyny P, Pokki JP, Pakkanen M, Keskinen KI |
29 - 35 |
Thermodynamic properties of the system NH4NO3+ (NH4)(2)SO4+ H2O at 298.15 K El Guendouzi M, Errougui A |
36 - 44 |
Volumetric properties of ethanol-water mixtures under high temperatures and pressures Pecar D, Dolecek V |
45 - 50 |
Liquid-liquid equilibria of water plus ethanol plus reformate de Doz MBG, Bonatti CM, Solimo HN |
51 - 57 |
Solubility of thiophene in carbon dioxide and carbon dioxide+1-propanol mixtures at temperatures from 313 to 363 K Elizalde-Solis O, Galicia-Luna LA |
58 - 63 |
Liquid-liquid equilibria of the ternary system water plus acetic acid plus dimethyl adipate Ince E |
64 - 71 |
Vapor pressures and apparent molal volumes of the solutions of ZnCl2 in ethanol at 298.15 K Sardroodi JJ, Zafarani-Moattar MT |
72 - 80 |
High pressure (solid plus liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction Morawski P, Coutinho JAP, Domanska U |
81 - 89 |
PVTx measurements for N2O+CH3F, N2O+CH2F2, and N2O+CHF3 binary systems Di Nicola G, Giuliani G, Polonara F, Stryiek R |
90 - 98 |
Method to determine quadruple points of a two-component system containing a simple hydrate phase and behavior of the system near these points Kiyono F, Tajima H, Ogasawara K, Yamasaki A |
99 - 104 |
Phase diagram for the system KVO3+NH4HCO3+NH4VO3+KHCO3+H(2)Oat303K Trypuc M, Kielkowska U |
105 - 108 |
Phase equilibria for binary systems of octane boosters with 2,2,4-trimethylpentane Reddy KVN, Prasad DHL, Krishnaiah A |
109 - 120 |
Revision of the volumetric method for measurements of liquid-liquid equilibria in binary systems Rehak K, Vonka P, Dreiseitlova J |
121 - 130 |
Liquid-liquid equilibria for pseudoternary systems: isooctane-benzene-(methanol plus water) Garcia-Flores BE, de Doz MG, Trejo A |
131 - 142 |
Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid-liquid-equilibria for binary systems of alkanes and aromatics with esters Collinet E, Gmehling J |
143 - 152 |
Phase-equilibrium calculations for non-aqueous and aqueous associating systems using continuous thermodynamics Browarzik D |
153 - 169 |
Enthalpy of dilution of (SO2 + H2O) and(SO2 + NH3+H2O) in pure water: experimental results and modeling Kamps APS, Meyer E, Ermatchkov V, Maurer G |
170 - 175 |
New regularities and an equation of state for liquids Goharshadi EK, Morsali A, Abbaspour M |
176 - 183 |
Solubility of polycyclic aromatics in binary solvent mixtures using activity coefficient models Ali SH, Al-Mutairi FS, Fahim MA |
184 - 191 |
Vapour-liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a)+dimethyl ether (DME) system at temperatures from 293.18 to 358.15 K and pressures up to about 3 MPa Valtz A, Gicquel L, Coquelet C, Richon D |
192 - 196 |
Studies on the properties of ionic liquid EMIInCl4 Zang SL, Zhang QG, Huang M, Wang B, Yang HZ |
197 - 203 |
Vapor-liquid equilibria and excess volumes of the binary systems ethanol plus ethyl lactate, isopropanol plus isopropyl lactate and n-butanol plus n-butyl lactate at 101.325 kPa Pena-Tejedor S, Murga R, Sanz MT, Beltran S |
204 - 205 |
Comment on the paper of Savaroglu and Aral entitled "Densities, speed of sound, and isentropic compressibilities of the ternary mixture 2-propanol plus acetone plus cyclohexane and constituent binary mixtures at 298.15 and 313.15 K" Zorebski E, Ernst S |
206 - 208 |
Reply to the letter to the editor by E. Zorebski, S. Ernst about the paper "Densities, speeds of sound and isentropic compressibilities of the ternary mixture 2-propanol plus acetone plus cyclohexane and the constituent binary mixtures at 298.15 and 313.15 K" [Fluid Phase Equilib. 215 (2004) 253-262] Savaroglu G, Aral E |
210 - 214 |
Revised solubility data and modeling of water in the gas phase of the methane/water binary system at temperatures from 283.08 to 318.12 K and pressures up to 34.5 MPa (vol 214, pg 101, 2003) Chapoy A, Coquelet C, Richon D |