1 - 6 |
Salt effects on extraction of trioxane from aqueous formaldehyde solutions Qi JG, Hu YF, Gao Y, Ma WT, Mo SQ, Yang ZY, Zhang XM, Yin LY |
7 - 20 |
Prediction of vapor-liquid and liquid-liquid equilibria at high pressures of 2-alkoxyethanol mixtures using PC-SAFT EoS NguyenHuynh D, Nguyen TT, Nguyen TTX |
21 - 43 |
Comparison of GERG-2008 and simpler EoS models in calculation of phase equilibrium and physical properties of natural gas related systems Varzandeh F, Stenby EH, Yan W |
44 - 48 |
Vapor-liquid distribution coefficients of hops extract in high pressure CO2 and ethanol mixtures and data correlation with entropy-based solubility parameters Ota M, Sugahara S, Sato Y, Smith RL, Inomata H |
49 - 62 |
Phase behavior experiments and PVT modeling of DME-brine-crude oil mixtures based on Huron-Vidal mixing rules for EOR applications Ratnakar RR, Dindoruk B, Wilson LC |
63 - 73 |
Thermodynamic solution properties of a biodegradable chelant (MGDA) and its interaction with the major constituents of natural fluids Bretti C, Cigala RM, De Stefano C, Lando G, Sammartano S |
74 - 86 |
Recommended vapor pressures for acenaphthylene, fluoranthene, and fluorene Mahnel T, Stejfa V, Fulem M, Ruzicka K |
87 - 92 |
Theoretical modeling of the thermodynamic properties and the phase diagram of binary gas hydrates of argon and hydrogen Zhdanov RK, Gets KV, Belosludov RV, Subbotin OS, Bozhko YY, Belosludov VR |
93 - 101 |
Alkane solubilities in aqueous alkanolamine solutions with CPA EoS Wang TY, El Ahmar E, Coquelet C |
102 - 106 |
Isobaric heat capacities of exo-tetrahydrodicyclopentadiene at temperatures from 323 K to 523 K and pressures up to 6 MPa Zhang Q, Liu XY, He MG |
107 - 116 |
Considering double occupancy of large cages in nitrogen and oxygen hydrates at high pressures Rasoolzadeh A, Shariati A |
117 - 129 |
Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics Srirachat W, Wannachod T, Pancharoen U, Kheawhom S |
130 - 140 |
Predicting PR EOS binary interaction parameter using readily available molecular properties Abudour AM, Mohammad SA, Robinson RL, Gasem KAM |
141 - 151 |
Measurement of the solubility of the salt of 2-mercaptobenzothiazole with cyclohexylamine and tert-butylamine in various solvents at low temperatures: Models and thermodynamic parameters Wongkaew K, Fulajtarova K, Hronec M, Mohdee V, Pancharoen U, Nootong K |
152 - 166 |
A priori determination of the region of the three physical volume root loci in the Perturbed-Chain SAFT EOS Alsaifi NM, Al Aslani I, Binous H, Wang ZG |
167 - 175 |
Solubility of alpha-glycine in water with additives at a temperature range of (293.15-343.15) K: Experimental data and results of thermodynamic modeling Sun H, Wang L, Liu BS |
176 - 192 |
Application of the modified Group-Contribution Perturbed-Chain SAFT to branched alkanes, n-olefins and their mixtures NguyenHuynh D, NguyenHuynh D |
193 - 199 |
Effect of temperature and diameter of narrow single-walled carbon nanotubes on the viscosity of nanofluid: A molecular dynamics study Vakili-Nezhaad G, Al-Wadhahi M, Gujrathi AM, Al-Maamari R, Mohammadi M |
200 - 210 |
Can the Boyle's and critical parameters be unambiguously correlated for polar and associating fluids, liquid metals, ionic liquids? Rogankov OV, Rogankov VB |
211 - 221 |
Vapor-liquid phase boundaries and swelling factors of C3H8-n-C4H10-CO2-heavy oil systems under reservoir conditions Li XL, Yang DY, Fan ZQ |
222 - 232 |
Phase equilibria calculations of electrolyte solutions containing water-polymer- salt using a new thermodynamic model, applicable in aqueous two phase systems Bakhshi H, Mobalegholeslam P |
233 - 243 |
Modeling the effect of piperazine on CO2 loading in MDEA/PZ mixture Ghalib L, Ali BS, Ashri WM, Mazari S, Saeed IM |