论文信息 - Vapor-liquid equilibria for binary mixtures of CO2 with 2-methyl-2-propanol, 2-methyl-2-butanol, octanoic acid, and decanoic acid at temperatures from 313.15 K to 353.15 K and pressures from 3 MPa to 24 MPa

Vapor-liquid equilibria for binary mixtures of CO2 with 2-methyl-2-propanol, 2-methyl-2-butanol, octanoic acid, and decanoic acid at temperatures from 313.15 K to 353.15 K and pressures from 3 MPa to 24 MPa

Phase behaviors of mixtures of CO 2 with 2-methyl-2-propanol, 2-methyl-2-butanol, octanoic acid, and decanoic acid were measured with a variable-volume view-cell apparatus from 313.15 K to 353.15 K and from 3 MPa to 24 MPa. The results were correlated by the multifluid-nonrandom lattice fluid (MF-NLF) equation of state.

[1] K. Yoo,et al. APPROXIMATE NONRANDOM TWO-FLUID LATTICE-HOLE THEORY. GENERAL DERIVATION AND DESCRIPTION OF PURE FLUIDS , 1997 .

[2] K. Yoo,et al. APPROXIMATE NONRANDOM TWO-FLUID LATTICE-HOLE THEORY. THERMODYNAMIC PROPERTIES OF REAL MIXTURES , 1997 .

[3] D. Combes,et al. Continuous reaction‐separation process for enzymatic esterification in supercritical carbon dioxide , 1994, Biotechnology and bioengineering.

[4] A. Russell,et al. STUDYING ENZYME ACTIVITY IN SUPERCRITICAL FLUIDS , 1994 .

[5] D. Combes,et al. Polar substrates for enzymatic reactions in supercritical CO2 : how to overcome the solubility limitation , 1994 .

[6] Takashi Katayama,et al. Isothermal Vapor-Liquid Equilibrium Data for Binary Systems Containing Carbon Dioxide at High Pressures: Methanol-Carbon Dioxide, n-Hexane-Carbon Dioxide, and Benzene-Carbon Dioxide Systems , 1976 .