High pressure vapor-liquid equilibria of four binary systems containing carbon dioxide.
スポンサーリンク
概要
- 論文の詳細を見る
Isothermal vapor-liquid equilibrium data of four binary systems -carbon dioxide+pentane at 311.15 and 329.15K, +diethyl ether at 313.15K, +methyl terf-butyl ether at 310.15, 329.15 and 338.15K, and +1-pentene at 303.15, 313.15 and 328.60 K-were determined by using an apparatus with vapor and liquid alternative circulation over a pressure range from 0.5 to 9.1 MPa. Experimental data were correlated by applying the Soave-Redlich-Kwong equation of state with the conventional quadratic mixing rule and the DDLC-EOS unified model based on the conformal reference state. Results show that both models correlate the present data satisfactorily.
- 公益社団法人 化学工学会の論文
著者
-
Zheng Xi-yin
Department Of Chemical Engineering Faculty Of Engineering Kyushu University
-
ZHENG XI-YIN
Department of Chemical Engineering, Dalian Institute of Technology, People''s Republic of China
-
KUBOTA HIRONOBU
Department of Chemical Engineering, Faculty of Engineering, Kobe University
-
MAKITA TADASHI
Department of Chemical Engineering, Faculty of Engineering, Kobe University
-
WU GUANG-WEN
Department of Chemical Engineering, Dalian Institute of Technology, People''s Republic of China
-
ZHANG NAI-WEN
Department of Chemical Engineering, Dalian Institute of Technology, People''s Republic of China
関連論文
- Comparison of Several Mixing Rules in Equations of State for Calculating Solid-Solubilities in Supercritical Fluids
- High pressure vapor-liquid equilibria of the HFC134a+HCFC123 system.
- Simplified and modified versions of the DDLC-EOS model.
- A unified model for strongly polar and asymmetric mixtures.
- Viscosity of binary gaseous mixtures of fluorocarbons.
- High pressure vapor-liquid equilibria of four binary systems containing carbon dioxide.
- Vapor-liquid equilibria of the ethylene-propylene system under high pressure.
- Viscosity of binary gaseous mixtures at moderate pressures - N2+He, N2+CClF3 (R13) and N2+CHClF2 (R22) systems.:N2+He, N2+CClF3 (R13) AND N2+CHClF2 (R22) SYSTEMS
- Vapor-liquid equilibria for the HCFC22+HCFC142b system.
- Viscosity of SF6+N2 and SF6+He gaseous mixtures.
- Thermal conductivity of gaseous methane and sulfur hexafluoride under pressure.
- Vapor-liquid equilibria of non-azeotropic halogenated hydrocarbon mixtures under high pressure.
- Thermodynamic properties of R13 (CClF3), R23 (CHF3), R152a (C2H4F2), and propane hydrates for desalination of sea water.
- Correlation of multiphase equilibria for asymmetric mixtures by a unified model.
- Density-dependent local-composition effects on mixing rule of cubic equations of state.