| 215 - 229 |
Studies on UNIQUAC and SAFT equations for nonionic surfactant solutions
Li XS, Lu JF, Li YG, Liu JC |
| 231 - 242 |
A saturated liquid density equation in conjunction with the Predictive-Soave-Redlich-Kwong equation of state for pure refrigerants and LNG multicomponent systems
Nasrifar K, Moshfeghian M |
| 243 - 249 |
Correlation of the extraction constants of the system Cd(II)-H3PO4/Cyanex 302-kerosene at different ionic strengths
Almela A, Elizalde MP |
| 251 - 263 |
Global approach for calculation of minimum miscibility pressure
Jessen K, Michelsen ML, Stenby EH |
| 265 - 277 |
Vapor-liquid equilibrium of binary mixtures of chlorobenzene with 3-methyl-1-butanol, 3-methyl-2-butanol and 2-methyl-2-butanol, at 100 kPa
Dejoz A, Gonzalez-Alfaro V, Llopis FJ, Miguel PJ, Vazquez MI |
| 279 - 292 |
Influence of temperature on the liquid-liquid equilibria containing two pairs of partially miscible liquids - Water plus furfural plus l-butanol ternary system
Marigliano ACG, de Doz MBG, Solimo HN |
| 293 - 315 |
Excess Gibbs energies of the ternary system ethanol plus N,N-dimethylformamide plus cyclohexane at 298.15 K
Lepori L, Matteoli E, Conti G, Gianni P |
| 317 - 340 |
Measurements of the heats of dilution and description of the system H2O/H2SO4/HCl with a solvation model
Rutten P, Kim SH, Roth M |
