| 189 - 199 |
Experimental vapor pressures and derived thermodynamic properties of aqueous solutions of lithium sulfate from 423 to 573 K
Abdulagatov IM, Azizov ND |
| 201 - 217 |
Wax phase equilibria: developing a thermodynamic model using a systematic approach
Ji HY, Tohidi B, Danesh A, Todd AC |
| 219 - 228 |
Multiphase equilibria for binary and ternary mixtures containing propionic acid, n-butanol, butyl propionate, and water
Lee MJ, Tsai LH, Hong GB, Lin HM |
| 229 - 233 |
Thermodynamic properties of the system NH4NO3-KNO3-H2O at 298.15 K
El Guendouzi M, Marouani M |
| 235 - 244 |
Viscosity and density of mixtures of methane and n-decane from 298 to 393 K and up to 75 MPa
Audonnet F, Padua AAH |
| 245 - 256 |
Excess volumes and isobaric heat capacities of diisopropyl ether with several alkanols at 298.15 K - Application of the symmetrical extended real associated solution model
Pineiro A |
| 257 - 270 |
The next generation of hydrate prediction IV - A comparison of available hydrate prediction programs
Ballard L, Sloan ED |
| 271 - 283 |
Phase equilibrium for the system rice bran oil plus fatty acids plus ethanol plus water plus gamma-oryzanol plus tocols
Rodrigues CEC, Pessoa PA, Meirelles AJA |
| 285 - 292 |
Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with cyclohexane at nine temperatures
Garriga R, Perez P, Gracia M |
| 293 - 299 |
Excess enthalpies of the ternary mixtures: tetrahydrofuran plus (diisopropyl ether or 2-methyltetrahydrofuran) plus n-heptane at 298.15 K
Wang ZH, Kodama D, Benson GC, Lu BCY |
| 301 - 305 |
Simplification and application of the mean spherical approximation (MSA) model for 1 : 1 electrolyte solution
Nakhaei GR, Modarress H |
| 307 - 321 |
Partial excess molar volumes, partial excess isentropic compressibilities and relative permittivities of water+ethane-1,2-diol derivative and water+1,2-dimethoxyethane at different temperatures
George J, Sastry NV |
