Fluid Phase Equilibria

Fluid Phase Equilibria, Vol.260, No.2 Entire volume, number list

ISSN: 0378-3812 (Print)

In this Issue (25 articles)

153 - 163	The third industrial fluid properties simulation challenge Case FH, Brennan J, Chaka A, Dobbs KD, Friend DG, Frurip D, Gordon PA, Moore J, Mountain RD, Olson J, Ross RB, Schiller M, Shen VK
164 - 168	Benchmarks for the third industrial fluid properties simulation challenge Gordon PA, Schiller M, Kao CPC, Bair S, Friend DG
169 - 176	State conditions transferability of vapor-liquid equilibria via fluctuation solution theory with correlation function integrals from molecular dynamics simulation Christensen S, Peters GH, Hansen FY, O'Connell JP, Abildskov J
177 - 182	Vapor pressure of R227ea+ethanol at 343.13 K by molecular simulation Eckl B, Huang YL, Vrabec J, Hasse H
183 - 189	Prediction, fine tuning, and temperature extrapolation of a vapor liquid equilibrium using COSMOtherm Klamt A, Eckert F
190 - 194	Modeling vapor-liquid equilibria of ethanol+1,1,1,2,3,3,3-heptafluoropropane binary mixtures using PC-SAFT Kleiner M, Sadowski G
195 - 198	Bubble point pressure estimates from Gibbs ensemble simulations Yazaydin AO, Martin MG
199 - 211	Prediction of the bubble point pressure for the binary mixture of ethanol and 1,1,1,2,3,3,3-heptafluoropropane from Gibbs ensemble Monte Carlo simulations using the TraPPE force field Rai N, Rafferty JL, Maiti A, Siepmann JI
212 - 217	Prediction of shear viscosities using periodic perturbation method and OPLS force field Zhao LF, Wang XJ, Wang L, Sun H
218 - 231	Prediction of viscosities and vapor-liquid equilibria for five polyhydric alcohols by molecular simulation Kelkar MS, Rafferty JL, Maginn EJ, Siepmann JI
233 - 247	From restricted towards realistic models of salt solutions: Corrected Debye-Huckel theory and Monte Carlo simulations Abbas Z, Ahlberg E, Nordholm S
248 - 261	Vapor pressure measurements in the range 10(-5) Pa to 1 Pa of four pentaerythritol esters - Density and vapor-liquid equilibria modeling of ester lubricants Razzouk A, Mokbel I, Garcia J, Femandez J, Msakni N, Jose J
262 - 265	Liquid-liquid equilibria of ternary mixture (propargyl alcohol plus diisopropyl ether plus water) Ye KM, Wu H, Deng G
266 - 274	Thermodynamic representation of phase equilibrium behavior of aqueous solutions of amino acids by the modified Wilson model Sadeghi R
275 - 278	The thermal conductivity of alumina nanoparticles dispersed in ethylene glycol Beck MP, Sun TF, Teja AS
279 - 286	Diffusion coefficients of 2-fluoroanisole, 2-bromoanisole, allylbenzene and 1,3-divinylbenzene at infinite dilution in supercritical carbon dioxide Suarez-Iglesias O, Medina I, Pizarro C, Bueno JL
287 - 294	Solubility of disperse yellow 54 in supercritical carbon dioxide with or without cosolvent Tsai CC, Lin HM, Lee MJ
295 - 299	The ternary system H2O-Fe(NO3)(3)-Co(NO3)(2) isotherms 0 and 15 degrees C El Goundali B, Kaddami M
300 - 315	Modelling of calcium sulphate solubility in concentrated multi-component Azimi G, Papangelakis VG, Dutrizac JE
316 - 325	Volume translation in equations of state as a means of accurate property estimation Frey K, Augustine C, Ciccolini RP, Paap S, Modell M, Tester J
326 - 334	Prediction of gas condensate properties by Esmaeilzadeh-Roshanfekr equation of state Bonyadi A, Esmaeilzadeh F
335 - 342	Apparent molar volume, isentropic compressibility and conductivity of di-sodium hydrogen phosphate in water and in aqueous solutions of 1-propanol Sadeghi R, Khoshnavazi R, Parhizkar H
343 - 353	A proposal for the estimation of binary mixture activity coefficients from surface tension measurements throughout the entire concentration range Broco P, Pineiro A, Amigo A, Gracia-Fadrique J
354 - 358	Binary interaction parameter k(ij) for calculating the second cross-virial coefficients of mixtures Meng L, Duan YY, Wang XD
359 - 359	Effect of temperature on the surface tension of diluted aqueous solutions of 1,2-hexanediol, 1,5-hexanediol, 1,6-hexanediol and 2,5-hexanediol (vol 258, pg 67, 2007) Romero CM, Paez MS, Miranda JA, Hernandez DJ, Oviedo LE