Phase equilibria for supercritical fluid process design
- 1 September 1989
- journal article
- review article
- Published by Wiley in AIChE Journal
- Vol. 35 (9), 1409-1427
- https://doi.org/10.1002/aic.690350902
Abstract
No abstract availableKeywords
This publication has 154 references indexed in Scilit:
- The excess enthalpies of (carbon dioxide + n-hexane + toluene) at 470.15 K and 7.50 and 12.50 MPaThe Journal of Chemical Thermodynamics, 1988
- High‐pressure solution behavior of the polystyrene‐toluene‐ethane systemAIChE Journal, 1988
- Application of a generalized multiproperty apparatus to measure phase equilibrium and vapor phase densities of supercritical carbon dioxide in n-hexadecane systems up to 26 MPaFluid Phase Equilibria, 1986
- Measurement of vapor-liquid equilibria at elevated temperatures and pressures using a flow type apparatusFluid Phase Equilibria, 1986
- Supercritical fluid processingEnvironmental Science & Technology, 1986
- A high-pressure-high-temperature chromatographic apparatus for the measurement of vapor-liquid equilibriaFluid Phase Equilibria, 1984
- Method for construction of nonclassical equations of stateFluid Phase Equilibria, 1983
- Supercritical fluid extraction with carbon dioxide and ethyleneFluid Phase Equilibria, 1983
- Selectivity of supercritical compounds and entrainers with respect to model substancesFluid Phase Equilibria, 1983
- Extraktion von Naturstoffen mit überkritischen und verflüssigten GasenMicrochimica Acta, 1980