1 - 6 |
(Solid plus liquid) phase equilibrium for the ternary system (K2CO3-Na2CO3-H2O) at T = (323.15, 343.15, and 363.15) K Yin CC, Liu MT, Yang J, Ma HW, Luo Z |
7 - 17 |
High pressure densities for mixed ionic liquids having different functionalities: 1-butyl-3-methylimidazolium chloride and 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide Hiraga Y, Koyama K, Sato Y, Smith RL |
18 - 25 |
Physico-chemical characterization antituberculosis thioacetazone: Vapor pressure, solubility and lipophilicity Sharapova A, Ol'khovich M, Blokhina S, Perlovich G |
26 - 37 |
Solubility and preferential solvation of some n-alkyl-parabens in methanol plus water mixtures at 298.15 K Cardenas ZJ, Jimenez DM, Delgado DR, Almanza OA, Jouyban A, Martinez F, Acree WE |
38 - 44 |
Thermodynamic and thermophysics properties of synthetic britholite SrPr4(SiO4)(3)O Knyazev AV, Bulanov EN, Smirnova NN, Korokin VZ, Shushunov AN, Blokhina AG, Xu ZY |
45 - 58 |
Solubility of 2-nitro-p-phenylenediamine in nine pure solvents and mixture of (methanol plus N-methyl-2-pyrrolidone) from T = (283.15 to 318.15) K: Determination and modelling Wang J, Xu AL, Xu RJ |
59 - 70 |
Determination of melting temperatures in hydrocarbon mixtures by differential scanning calorimetry Oakley JH, Hughes TJ, Graham BF, Marsh KN, May EF |
71 - 75 |
Interfacial tension between (methane plus ethane plus propane) gas mixture and water from 283.2 K to 298.2 K under up to 10 MPa Hayama H, Fukuzawa K, Yasuda K, Ohmura R |
76 - 83 |
Thermodynamic equilibrium of hydroxyacetic acid in pure and binary solvent systems Huang QY, Xie C, Li Y, Su NN, Lou YJ, Hu XX, Wang YL, Bao Y, Hou BH |
84 - 96 |
Experimental determination of the critical loci for R-23+(n-propane or n-hexane) and R-116+n-propane binary mixtures Williams-Wynn MD, El Abbadi J, Valtz A, Kovacs E, Houriez C, Naidoo P, Coquelet C, Ramjugernath D |
97 - 104 |
Binary and ternary solid-liquid phase equilibrium for the systems formed by succinic acid, urea and diethylene glycol: Determination and modelling Li YX, Li CC, Han S, Zhao HK |
105 - 117 |
Phase behaviour at different temperatures of ionic liquid based aqueous two-phase systems containing {[Bmim]BF4 + salt sulfate (Zn2+ or Ni2+) + water) Aguiar CD, Machado PAL, Alvarenga BG, Lemes NHT, Virtuoso LS |
118 - 126 |
Fractionation of acid lime essential oil using ethanol/water mixtures: Effect of the process on the aroma profile Goncalves D, Costa P, Rodrigues CEC, Rodrigues AE |
127 - 135 |
Liquid-liquid separation of hex-1-ene from hexane and cyclohexene from cyclohexane with ionic liquids Karpinska M, Wlazlo M, Domanska U |
136 - 142 |
Aqueous two-phase systems with therrno-sensitive EOPO co-polymer (UCON) and sulfate salts: Effect of temperature and cation Rico-Castro X, Gonzalez-Amado M, Soto A, Rodriguez O |
143 - 144 |
Calculation of excess Gibbs energy of activation for viscous flow in (ionic liquid plus co-solvent) Heitz MP |
145 - 161 |
Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods Nain AK, Chaudhary N, Ankita, Gupta J, Chandra P |
162 - 180 |
Volumetric and viscometric properties of binary liquid mixtures as potential solvents for flue gas desulfurization processes Zivkovic NV, Zivkovic EM, Serbanovic SP, Majstorovic DM, Kijevcanin ML |
181 - 192 |
Molecular interaction between binary mixtures 1-butyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)imide with N-Vinyl-2-pyrrolidinone at different temperatures Suneetha P, Krishna TS, Gowrisankar M, Ravindhranath K, Ramchandran D |
193 - 198 |
The investigation on the vapour liquid phase equilibrium of (ammonia+1,1,1,2-tetrafluoroethane) system over the temperatures ranging from (243.150 to 283.150) K Zhao YX, Dong XQ, Zhong Q, Gong MQ, Shen J |
199 - 201 |
Commentary on "thermodynamic equilibrium of hydroxyacetic acid in pure and binary solvent systems" Acree WE |