1 - 6 |
Phase behavior of xenon hydrate system Ohgaki K, Sugahara T, Suzuki M, Jindai H |
7 - 18 |
Measurement of water activities and prediction of liquid-liquid equilibria for water plus ethylene oxide-propylene oxide random copolymer plus ammonium sulfate systems Li W, Lin DQ, Zhu ZQ |
19 - 33 |
High pressure phase equilibrium data for the systems carbon dioxide/ethyl acetate and carbon dioxide/isoamyl acetate at 295.2, 303.2 and 313.2 K da Silva M, Barbosa D, Ferreira PO, Mendonca J |
35 - 43 |
Excess chemical potentials, partial molar enthalpies and entropies in binary aqueous acetone and tetramethyl urea at 25 degrees C Chen DHC, Chu PM, Tanaka SH, To ECH, Koga Y |
45 - 52 |
High-pressure phase equilibria and thermodynamic modelling for the binary systems CO2+lemon oil and C2H6+lemon oil de la Fuente JC, Bottini SB |
53 - 61 |
Solubility of H2S and CO2 in diethylene glycol at elevated pressures Jou FY, Otto FD, Mather AE |
63 - 73 |
Speeds of sound and isentropic compressibilities of (n-heptanol plus n-pentane, or n-hexane, or n-heptane, or n-octane) at T=303.15 K, and of (n-heptanol+2,2,4-trimethylpentane) at T=293.15 and 303.15 K Nath J |
75 - 89 |
Measurement and prediction of phase equilibria for water plus CO2 in hydrate forming conditions Yang SO, Yang IM, Kim YS, Lee CS |
91 - 105 |
Isobaric vapor-liquid equilibria of alkyl carbonates with alcohols Luo HP, Xiao WD, Zhu KH |
107 - 115 |
Vapor-liquid equilibria of carbon dioxide with linoleic acid, alpha-tocopherol and triolein at elevated pressures Chen CC, Chang CMJ, Yang PW |
117 - 124 |
Vapor-liquid equilibria for the ternary system benzene plus n-heptane plus N,N-dimethylformamide at 101.33 kPa Blanco B, Sanz MT, Beltran S, Cabezas JL, Coca J |
125 - 138 |
Isobaric vapor-liquid equilibrium for binary and ternary mixtures of 2-methyl-2-propanol plus methyl 1,1-dimethylpropyl ether plus 2,2,4-trianethylpentane Loras S, Aucejo A, Munoz R, de la Torre J |
139 - 152 |
Vapor-liquid equilibria for binary mixtures of nitroethane with aliphatic alcohols (C-1-C-4) at 101.3 kPa Tu CH, Wang WF, Hsian HY, Chou YT |
153 - 174 |
Isochoric heat capacity measurements of nitrogen tetroxide system at temperatures between 410 and 484 K and pressures up to 35 MPa Polikhronidi NG, Batyrova RG, Abdulagatov IM |
175 - 183 |
Isothermal gravitational segregation: algorithms and specifications Halldorsson S, Stenby EH |
185 - 196 |
A surface tension model for liquid mixtures based on the Wilson equation Li CX, Wang WC, Wang ZH |
197 - 212 |
Modelling of the equilibrium properties of the system H3PO4-H2O: representation of VLE and liquid phase composition Cherif M, Mgaidi A, Ammar MN, Abderrabba M, Furst W |
213 - 228 |
New local composition model for electrolyte solutions: multicomponent systems Jaretun A, Aly G |
229 - 236 |
The Bancroft point and vapor-liquid equilibria in the system benzene plus isopropanol Elliott JR, Rainwater JC |
237 - 251 |
Determination of ISM equation of state for liquids from surface energy: a simplified procedure for mixtures Ghatee MH, Farsi M |
253 - 272 |
Global phase stability analysis for heterogeneous reactive mixtures and calculation of reactive liquid-liquid and vapor-liquid-liquid equilibria Wasylkiewicz SK, Ung S |
273 - 284 |
Calculation of the Joule-Thomson inversion curves from cubic equations of state Matin NS, Haghighi B |
285 - 310 |
Extension of the electrolyte EOS of Furst and Renon to mixed solvent electrolyte systems Zuo JYX, Zhang D, Furst W |
311 - 323 |
A new method for predicting saturated liquid viscosity at temperatures above the normal boiling point Sastri SRS, Rao KK |
325 - 325 |
Reply to'Comment on "Vapor-liquid equilibria in porous media"' Shin YO, Simandl J |