1 - 15 |
Totally inclusive cubic equation of state with five parameters for pure fluids Sun JX |
17 - 28 |
Experimental determination of methane hydrate stability in methanol and electrolyte solutions Jager MD, Peters CJ, Sloan ED |
29 - 39 |
Phase equilibria of 1,1,1-trifluoroethane (HFC-143a)+1,1,1,2-tetrafluoroethane (HFC-134a), and +1,1-difluoroethane (HFC-152a) at 273.15, 293.15, 303.15, and 313.15 K Lim JS, Park JY, Lee BG, Lee YW |
41 - 51 |
Solubility of xenon in n-hexane between 257 and 333 K Bonifacio RP, Gomes MFC, Filipe EJM |
53 - 73 |
Activity coefficient prediction by osmotic molecular dynamics Crozier PS, Rowley RL |
75 - 86 |
Universal method for equations of state (UNIFEST) - An application of UNIFAC to predict the parameters of cubic equations of state Soave GS |
87 - 95 |
Excess properties of liquid mixtures from the perturbation theory of Barker-Henderson Koyuncu M, Demirtas A, Ogul R |
97 - 107 |
Correlation, verification and prediction of vapour-liquid equilibria using equation of state with association term II. Alcohols plus non-aliphatic hydrocarbons Goral M |
109 - 121 |
Isothermal vapor-liquid equilibria and excess molar volumes for the ternary mixtures containing 2-methyl pyrazine Park SJ, Han KJ, Choi MJ, Gmehling J |
123 - 133 |
Phase equilibria for liquid mixtures of (butanenitrile plus a carboxylic acid plus water) at 298.15 K Letcher TM, Redhi GG |
135 - 145 |
Effect of nonvolatile solute on vapor-liquid equilibrium at fixed liquid composition Sun RY, Sun Q |
147 - 165 |
Predicting the dew point pressure for gas condensate reservoirs: empirical models and equations of state Elsharkawy AM |
167 - 177 |
Prediction of the thermodynamic properties of quinary liquid alloys by modified coordination equation Tao DP, Yang B, Li DF |
179 - 189 |
Molecular dynamics study on homonuclear and heteronuclear chains of Lennard-Jones segments Banaszak M, Radosz M |
191 - 201 |
Solubility of anthracene in two binary solvents containing toluene Al-Sharrah GK, Ali SH, Fahim MA |
203 - 216 |
FT-IR study on interactions between solutes and entrainers in supercritical carbon dioxide Iwai Y, Tanabe D, Yamamoto M, Nakajima T, Uno M, Arai Y |
217 - 227 |
Liquid-liquid equilibria for methanol plus hexadecane plus heterocyclic nitrogen-containing compounds at 298.15 K Won DB, Park SJ, Han KJ, Kim CJ |
229 - 243 |
Thermodynamic modeling and experimental verification for ion-exchange synthesis of K2O center dot 6TiO(2) and TiO2 fibers from K2O center dot 4TiO(2) Bao NZ, Lu XH, Ji XY, Feng X, Xie JW |
245 - 259 |
Gas hydrate phase equilibria for propane in the presence of additive components Mooijer-van den Heuvel MM, Peters CJ, Arons JD |
261 - 275 |
Liquid-liquid equilibria of water-hydrocarbon systems from cubic equations of state Nasrifar K, Moshfeghian M |
277 - 287 |
Theory and computer simulation of the coordination number of square-well fluids of variable width Largo J, Solana JR |
289 - 301 |
Vapor-liquid equilibrium of octane-enhancing additives in gasolines - 4. Total pressure data and G(E) for ternary mixtures containing isopropyl ether or benzene and n-heptane+1-hexene at 313.15 K Chamorro CR, Segovia JJ, Martin MC, Villamanan MA |
303 - 308 |
Thermophysical conditions of phase equilibrium in a liquid-vapour system and correlation of thermodynamic parameters at the critical point Galibin N |