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- W1599691725 abstract "Gibbs-Duhem equation was applied to make the thermodynamic consistency test and the thermodynamic model estimation for CO2/DME, DME/CH3OH, CO2/CH3OH and DME/C2H5OH on the basis of the vapor-liquid equilibrium experimental data referred. The study shows that the PR-NRTL model combination is reasonable for the above four systems. Then, the NRTL binary interaction-parameters of the above systems were regressed from the vapor-liquid equilibrium data evaluated by the thermodynamic consistency test and the PR-NRTL model combination was emploied with the new parameters to calculate the vapor-liquid equilibrium for CH3OH/DME/CO2 at the temperature of 313.15 K and 333.15 K. Compared with the experimental data, the calculated deviation is small. On the basis of the above study, the vapor-liquid equilibrium in the system C2H5OH/DME/CO2 was estimated and the phase diagrams of the system was presented." @default.
- W1599691725 created "2016-06-24" @default.
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- W1599691725 date "2004-10-10" @default.
- W1599691725 modified "2023-09-27" @default.
- W1599691725 title "CO2／DME／CH3OH和CO2／DME／C2H5OH体系的汽液相平衡研究" @default.
- W1599691725 hasPublicationYear "2004" @default.
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