화학공학소재연구정보센터
검색결과 : 26건
No. Article
1 Extending the Range of COSMO-SAC to High Temperatures and High Pressures
Silveira CL, Sandler SI
AIChE Journal, 64(5), 1806, 2018
2 Prediction of solid-liquid-gas equilibrium for binary mixtures of carbon dioxide plus organic compounds from approaches based on the COSMO-SAC model
Chen CY, Wang LH, Hsieh CM, Lin ST
Journal of Supercritical Fluids, 133, 318, 2018
3 Modeling phase equilibrium with a modified Wong-Sandler mixing rule for natural gas hydrates: Experimental validation
Thakre N, Jana AK
Applied Energy, 205, 749, 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 Measurement and correlation of the isothermal VLE data for the binary mixtures of cyclopentene (CPEN)+cyclopentyl methyl ether (CPME)
Jeong WJ, Lim JS
Korean Journal of Chemical Engineering, 34(2), 463, 2017
6 Prediction of vapor-liquid equilibria for mixtures of low boiling point compounds using Wong-Sandler mixing rule and EOS/G(E) model
Espanani R, Miller A, Jacoby W
Chemical Engineering Science, 152, 343, 2016
7 Phase behavior of the CO2-H2O system at temperatures of 273-623 K and pressures of 0.1-200 MPa using Peng-Robinson-Stryjek-Vera equation of state with a modified Wong -Sandler mixing rule: An extension to the CO2-CH4-H2O system
Zhao HN, Lvov SN
Fluid Phase Equilibria, 417, 96, 2016
8 Vapor-liquid equilibria for the binary mixtures of methanol+cyclopentyl methyl ether (CPME)
Jeong WJ, Cho HK, Lim JS
Korean Journal of Chemical Engineering, 33(10), 2961, 2016
9 Thermodynamic Consistency Test for Binary Gas plus Water Equilibrium Data at Low and High Pressures
Faundez CA, Quiero FA, Valderrama JO
Chinese Journal of Chemical Engineering, 21(10), 1172, 2013
10 Measurement and correlation of the isothermal vapor-liquid equilibrium data for carbon dioxide and dimethyl ether system
Lee MH, Yim JH, Lim JS
Korean Journal of Chemical Engineering, 29(10), 1418, 2012