1 - 8 |
High-pressure phase equilibria of binary and ternary mixtures of carbon dioxide, triglycerides and free fatty acids: Measurement and modeling with the GC-EOS Fernandez-Ronco MP, Cismondi M, Gracia I, De Lucas A, Rodriguez JF |
9 - 16 |
Modeling of high-pressure vapor liquid equilibrium in ionic liquids plus gas systems using the PRSV equation of state Arce PF, Robles PA, Graber TA, Aznar M |
17 - 25 |
Infinite dilution activity coefficient and vapour liquid equilibrium measurements for dimethylsulphide and tetrahydrothiophene with hydrocarbons Haimi P, Uusi-Kyyny P, Pokki JP, Alopaeus V |
26 - 37 |
Relationship between the binary interaction parameters (k(ij)) of the Peng-Robinson and those of the Soave-Redlich-Kwong equations of state: Application to the definition of the PR2SRK model Jaubert JN, Privat R |
38 - 45 |
A new cubic equation of state for prediction of VLE of polymer solutions Staudt PB, Soares RD, Secchi AR, Cardozo NSM |
46 - 49 |
Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate Zhao GJ, Bi SS, Li X, Wu JT |
50 - 59 |
An analytical perturbed equation of state for hard chain fluids: Application to n-alkanes and n-perfluoroalkanes Farrokhpour H, Massoudi M |
60 - 67 |
Dependency of thermal and electrical conductivity on temperature and composition of Sn in Pb-Sn alloys Ocak Y, Aksoz S, Marasli N, Cadirli E |
68 - 75 |
Densities and electrical conductances of amino acids plus ionic liquid ([HMIm]Br) + H2O mixtures at 298.15 K Shekaari H, Jebali F |
76 - 92 |
Are safe results obtained when the PC-SAFT equation of state is applied to ordinary pure chemicals? Privat R, Gani R, Jaubert JN |
93 - 97 |
Liquid-liquid equilibrium in ternary ionic liquid systems by UNIFAC: New volume, surface area and interaction parameters. Part I Santiago RS, Santos GR, Aznar M |
98 - 103 |
Liquid-liquid equilibria of ionic liquid 1-butyl-3-methylimidazolium tetrafluoroborate and sodium citrate/tartrate/acetate aqueous two-phase systems at 298.15 K: Experiment and correlation Han JA, Yu CL, Wang Y, Xie XQ, Yan YS, Yin GW, Guan WX |
104 - 124 |
Thermodynamic model of aqueous CO2-H2O-NaCl solutions from-22 to 100 degrees C and from 0.1 to 100 MPa Akinfiev NN, Diamond LW |
125 - 129 |
Phase equilibria for benzene-cyclohexene and activity coefficients at infinite dilution for the ternary systems with ionic liquids Cehreli S, Gmehling J |
130 - 136 |
Phase equilibrium and thermophysical properties of mixtures containing a cyclic ether and 1-chloropropane Nonay N, Giner I, Giner B, Artigas H, Lafuente C |
137 - 147 |
Phase behaviors for the supercritical ethylene+1-hexene + hexane plus polyethylene systems at elevated temperatures and pressures Haruki M, Mano S, Koga Y, Kihara S, Takishima S |
148 - 150 |
Reply to comments of Endo and Goss concerning "development of correlations for describing solute transfer into acyclic alcohol solvents based on the Abraham model and fragment-specific equation coefficients" Grubbs LM, Achi SS, Acree WE, Abraham MH |
151 - 151 |
Prediction of phase equilibrium in mixtures containing ionic liquids using UNIFAC (vol 284, pg 99, 2009) Alevizou EI, Pappa GD, Voutsas EC |
152 - 153 |
Isobaric thermal expansivity of the binary system 1-hexanol + n-hexane as a function of temperature and pressure (vol 276, pg 1, 2009) Navia P, Troncoso J, Romani L |