Abstract
A new flow-type apparatus was developed using an overflow-type liquid level self-control system and a back pressure regulator. The present apparatus makes possible vapor-liquid equilibrium measurements at high temperatures by minimizing the residence time of heat-sensitive substances. It was shown that the resulting vapor-and liquid-phase compositions were independent of the sample flow rate within the range of flow rates employed. Vapor-liquid equilibrium data were measured with this apparatus for the systems C02-«-heptane, C02-«-decane, C02-trans-decaIin, C02-tetralin, C02-quinoline, benzene-tetralin and benzene-quinoline in the temperature range from 340 to 710 K at several pressures up to 23 MPa.
Original language | English |
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Pages (from-to) | 386-391 |
Number of pages | 6 |
Journal | Journal of Chemical Engineering of Japan |
Volume | 19 |
Issue number | 5 |
DOIs | |
Publication status | Published - 1986 |
Keywords
- Flow Type
- High Pressure
- High Temperature
- Phase Equilibrium
- Thermodynamics