1 - 12 |
Speeding up the two-phase PT-flash, with applications for calculation of miscible displacement Michael ML |
13 - 27 |
Simulations in ternary hard sphere mixtures Sindelka M, Boublik T |
29 - 39 |
Estimation of the critical constants of heavy hydrocarbons for their treatment by the Soave-Redlich-Kwong equation of state Soave GS |
41 - 63 |
Thermodynamic properties of binary mixtures of tetrachloromethane+n-alcohol by application of the dispersive quasichemical model Kechavarz R, Guigue JP, Tachoire H, Kenz A, Sbai K |
65 - 69 |
Prediction of the critical pressure of hydrocarbon mixtures by using the properties of pure substances Liu ZY, Zou J, Hu LN |
71 - 82 |
Prediction of vapor-liquid equilibria for asymmetric systems at low and high pressures with the PSRK model Li JD, Fischer K, Gmehling J |
83 - 88 |
A new combining rule for mixture equations of state : higher order composition dependencies reduce to quadratic composition dependence. Application to natural gas mixtures Luongo-Ortiz JF, Starling KE |
89 - 98 |
A correction to Sandler-Wong mixing rules Satyro MA, Trebble MA |
99 - 109 |
Phase behaviour of mixtures containing antibiotics - Effect of hydrogen bonding on tetracycline partitioning Kumar R, Betageri GV, Gupta RB |
111 - 123 |
Thermodynamic properties of n-alkoxyethanols plus organic solvents mixtures - VIII. Liquid-liquid equilibria of systems containing 2-methoxyethanol and alkanes (C6H12 and CH3-(CH2)(u)-CH3, u=3, 4, 6, 8) Rubio MA, Gonzalez JA, de la Fuente IG, Cobos JC |
125 - 141 |
Vapor-liquid equilibria for the systems propane+m-cresol, propane+p-cresol, and propane+m-cresol+p-cresol at high pressures Lee KR, Tan CS |
143 - 152 |
New applications of the ERAS-Model : excess volumes of binary liquid mixtures of 1-alkanols with acetonitrile Pina CG, Francesconi AZ |
153 - 161 |
Excess molar Gibbs energies of 2-methylpropan-1-ol with benzene or toluene or o- or m- and p-xylene at 308.15K in terms of an association model Bhardwaj U, Maken S, Singh KC |
163 - 172 |
Solubilities of 1-propanol and 1,2-propanediol in supercritical carbon dioxide. New analytical procedure and measurements Chylinski K, Gregorowicz J |
173 - 184 |
The effects of selected solvents on the relative volatility of a binary system consisting of 1-octene and 2-hexanone Everson RC, van der Merwe BJ |
185 - 203 |
The effect of the addition of water, propane, or docosane on the vapour-liquid and solid-fluid equilibria in asymmetric binary n-alkane mixtures Floter E, Hollanders B, de Loos TW, Arons JD |
205 - 211 |
Phase equilibria of supercritical propane Fengcheng bitumen system and the density and viscosity of the liquid phase Han BX, Yang GY, Ke J, Mao C, Yan HK |
213 - 239 |
Measurements of heat capacities at constant volume for aqueous salt solutions (H2O+NaCl, H2O+KCl and H2O+NaOH) near the critical point of pure water Abdulagatov IM, Dvoryanchikov VI, Mursalov BA, Kamalov AN |
241 - 251 |
Excess molar volumes and viscosities of binary mixtures of 2-(2-butoxyethoxy)ethanol with chloroalkanes at 298.15K Pal A, Kumar A |
253 - 262 |
Viscosities and densities of eight binary 1-alkanol systems at 308.15 and 313.15 K Shan ZJ, Asfour AFA |
263 - 274 |
Viscometric properties of multicomponent liquid n-alkane systems Wu JN, Shan ZJ, Asfour AFA |