Abstract
Phase compositions for gas-liquid equilibrium have been measured for ternary ethand-water-C02 mixtures at temperatures of 35, 50, and 65 °C and pressures of 10.2, 13.6, and 17.0 MPa. The experimental results can be used to characterize the solvent properties of dense C02 in the extraction of ethanol from aqueous solutions.
Original language | English (US) |
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Pages (from-to) | 296-298 |
Number of pages | 3 |
Journal | Journal of Chemical and Engineering Data |
Volume | 31 |
Issue number | 3 |
DOIs | |
State | Published - 1986 |
Externally published | Yes |
ASJC Scopus subject areas
- General Chemistry
- General Chemical Engineering