| 1 |
Vapor liquid equilibria for binary mixtures of difluoromethane (R32) + fluoroethane (R161) and fluoroethane (R161) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
Meng XY, Hu XZ, Yang T, Wu JT
Journal of Chemical Thermodynamics, 118, 43, 2018 |
| 2 |
Isothermal vapor liquid equilibrium measurements for difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
Hu XZ, Meng XY, Wu JT
Fluid Phase Equilibria, 431, 58, 2017 |
| 3 |
Vapor liquid equilibrium measurements for difluoromethane (R32)+2,3,3,3-tetrafluoroprop-1-ene (R1234yf) and fluoroethane (R161)+2,3,3,3-tetrafluoroprop-1-ene (R1234yf)
Hu XZ, Yang T, Meng XY, Bi SS, Wu JT
Fluid Phase Equilibria, 438, 10, 2017 |
| 4 |
Modeling vapor-liquid phase equilibria of methane-water and methane-carbon dioxide-water systems at 274K to 573K and 0.1 to 150 MPa using PRSV equation of state and Wong-Sandler mixing rule
Zhao HN
Fluid Phase Equilibria, 447, 12, 2017 |
| 5 |
Comparison between the artificial neural network, SAFT and PRSV approach in obtaining the solubility of solid aromatic compounds in supercritical carbon dioxide
Vaferi B, Karimi M, Azizi M, Esmaeili H
Journal of Supercritical Fluids, 77, 44, 2013 |
| 6 |
The iPRSV equation of state
van der Stelt TP, Nannan NR, Colonna P
Fluid Phase Equilibria, 330, 24, 2012 |
| 7 |
Excess molar volume, viscosity, and refractive index study for the ternary mixture {2-methyl-2-butanol (1) + tetrahydrofuran (2) + propylamine (3)} at different temperatures. Application of the ERAS-model and Peng-Robinson-Stryjek-Vera equation of state
Fattahi M, Iloukhani H
Journal of Chemical Thermodynamics, 42(11), 1335, 2010 |
| 8 |
Rapid one-step construction of hairpin RNA
Yan P, Shen WT, Gao XZ, Duan J, Zhou P
Biochemical and Biophysical Research Communications, 383(4), 464, 2009 |
| 9 |
Modelling of the phase behaviour for the direct synthesis of dimethyl carbonate from CO2 and methanol at supercritical or near critical conditions
Pinero R, Garcia J, Sokolova M, Cocero MJ
Journal of Chemical Thermodynamics, 39(4), 536, 2007 |
| 10 |
A new model and extension of Wong-Sandler mixing rule for prediction of (vapour plus liquid) equilibrium of polymer solutions using EOS/G(E)
Haghtalab A, Espanani R
Journal of Chemical Thermodynamics, 36(10), 901, 2004 |
