High-pressure phase equilibria of the system CO2—water—acetone measured with a new apparatus
- 31 December 1990
- journal article
- Published by Elsevier in Chemical Engineering Science
- Vol. 45 (3) , 751-758
- https://doi.org/10.1016/0009-2509(90)87016-l
Abstract
No abstract availableKeywords
This publication has 12 references indexed in Scilit:
- High-Pressure Phase Equilibria in Ternary Fluid Mixtures with a Supercritical ComponentPublished by American Chemical Society (ACS) ,1987
- Compilation of parameters for a polar fluid Soave-Redlich-Kwong equation of stateIndustrial & Engineering Chemistry Process Design and Development, 1986
- Vapor-liquid equilibriums for the carbon dioxide-1-butene system at 37.7 and 45.0.degree.CJournal of Chemical & Engineering Data, 1983
- Rapid computation of binary interaction coefficients of an equation of state for vapor—liquid equilibrium calculations. Application to the Redlich—Kwong—Soave equation of stateFluid Phase Equilibria, 1981
- Das isotherme Dampf-Flüssigkeits-Phasengleichgewichtsverhalten des Systems Aceton/Wasser bei 35° CZeitschrift für Physikalische Chemie, 1979
- New mixing rules in simple equations of state for representing vapour-liquid equilibria of strongly non-ideal mixturesFluid Phase Equilibria, 1979
- ISOTHERMAL VAPOR-LIQUID EQUILIBRIA OF ACETONE-CARBON DIOXIDE AND METHANOL-CARBON DIOXIDE SYSTEMS AT HIGH PRESSURESJOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1975
- A high pressure autocollimating refractometer for determining coexisting liquid and vapor phase densitiesThe Canadian Journal of Chemical Engineering, 1971
- The n-Butane–Carbon Dioxide SystemIndustrial & Engineering Chemistry, 1949
- Phase Behavior of Binary Carbon Dioxide-Paraffin SystemsIndustrial & Engineering Chemistry, 1945