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Two-Phase Equilibrium in Binary and Ternary Systems. IV. The System Ethane-Propylene

H. Lu, D. M. Newitt and M. Ruhemann
Proceedings of the Royal Society of London. Series A, Mathematical and Physical Sciences
Vol. 178, No. 975 (Aug. 15, 1941), pp. 506-525
Published by: Royal Society
Stable URL: http://www.jstor.org/stable/97533
Page Count: 20
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Since scans are not currently available to screen readers, please contact JSTOR User Support for access. We'll provide a PDF copy for your screen reader.
Two-Phase Equilibrium in Binary and Ternary Systems. IV. The System Ethane-Propylene
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Abstract

The liquid-vapour equilibrium of the binary system ethane-propylene has been determined at a number of temperatures between - 30 and 70° C and over a wide pressure range. From dew-point, boiling-point and pressure-volume-temperature measurements the (P, T)x, (T, x)P and (P, V)x, T relationships for the pure hydrocarbons and for nine mixtures have been determined.

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