Vapor-liquid equilibrium in the carbon dioxide-propylene carbonate system at high pressures

Journal of Chemical and Engineering Data

Volumn 47, Issue 2, 2002, Pages 282-285

  Williams, Laurie L ^a   Mas, Eric M ^a   Rubin, James B ^a  

^a LOS ALAMOS NATIONAL LABORATORY   (United States)

Author keywords

[No Author keywords available]

Indexed keywords

INTERACTION PARAMETERS;

CARBON DIOXIDE; CARBONATES; EQUATIONS OF STATE; ISOTHERMS; PHASE EQUILIBRIA; PRESSURE EFFECTS; PROPYLENE;

BINARY MIXTURES;

EID: 0036500194     PISSN: 00219568     EISSN: None     Source Type: Journal    
DOI: 10.1021/je010151x     Document Type: Article

References (13)

1. Equilibrium constants from a modified redlich-kwong equation of state
2. Mixing rules for cubic equations of state. Applications for supercritical fluid extraction modeling
3. 2/propylene carbonate in supercritical fluid chromatography
4. Solubility of carbon dioxide in propylene carbonate at elevated pressures and higher than ambient temperature
5. Phase equilibria and volume relationships in the system propylene carbonate-carbon dioxide
6. Isothermal vapor-liquid equilibria for systems ethyl ether-carbon dioxide and methyl acetate carbon dioxide at high pressures
7. Vapor-liquid equilibrium in the carbon dioxide-ethyl acetate system at high pressure
8. Phase equilibria for enzyme-catalyzed reactions in supercritical carbon dioxide
9. High-pressure phase equilibrium data for the systems carbon dioxide/ethyl acetate and carbon dioxide/isoamyl acetate at 295.2, 303.2, and 313.2 K
10. Vapor-liquid at high pressure in the system containing carbon dioxide and propyl acetate
11. Vapor-liquid in the carbon dioxide-ethyl propanoate system at pressures from 2 to 9 MPa and temperatures from 303 to 323K
12. Vapor-liquid equilibria for binary mixtures of carbon dioxide and fatty acid methyl esters