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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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Lu et al. (1941) studied this question.
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