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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