| 1 |
Calculation of density, vapor pressure and heat capacity near the critical point by incorporating cubic SRK EoS and crossover translation
Saeed A, Ghader S
Fluid Phase Equilibria, 493, 10, 2019 |
| 2 |
Phase equilibria of CO2+1,2-dimethoxyethane at high-pressures
Sima S, Secuianu C, Feroiu V
Fluid Phase Equilibria, 458, 47, 2018 |
| 3 |
Solubility of carbon dioxide in methanol from 213.15 K to 273.15 K: Measurement and modeling
Lyu ZX, Ma HF, Zhang HT, Ying WY
Fluid Phase Equilibria, 471, 40, 2018 |
| 4 |
A new viscosity model based on Soave-Redlich-Kwong equation of state
Bonyadi M, Rostami M
Fluid Phase Equilibria, 451, 40, 2017 |
| 5 |
Solubility of carbon monoxide in bio-oil compounds
Qureshi MS, Le Nedelec T, Guerrero-Amaya H, Uusi-Kyyny P, Richon D, Alopaeus V
Journal of Chemical Thermodynamics, 105, 296, 2017 |
| 6 |
Comparison of SRK and CPA equations of state for phase equilibrium of binary and ternary systems containing aromatics
Mahmoudjanloo H, Izadpanah AA, Rajaei H, Karamian S, Esmaeilzadeh F
Fluid Phase Equilibria, 408, 38, 2016 |
| 7 |
Quantitative comparison between predicted and experimental binary n-alkane plus benzene phase behaviors using cubic and PC-SAFT EOS
Ahitan S, Shaw JM
Fluid Phase Equilibria, 428, 4, 2016 |
| 8 |
Phase behavior of the carbon dioxide+1-dodecanol system,at high pressures
Secuianu C, Feroiu V, Geana D
Fluid Phase Equilibria, 428, 62, 2016 |
| 9 |
Modelling fluid phase equilibria in the binary system trifluoromethane+1-phenylpropane
Bogatu C, Duta A, de Loos TW, Geana D
Fluid Phase Equilibria, 428, 190, 2016 |
| 10 |
High pressures phase equilibria of (carbon dioxide+1-undecanol) system and their potential role in carbon capture and storage
Secuianu C, Ionita S, Feroiu V, Geana D
Journal of Chemical Thermodynamics, 93, 360, 2016 |
