1986
DOI: 10.1021/je00044a011
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Vapor-liquid critical curve of the system ethane + 2-methylpropane

Abstract: The vapor-liquid critical curve of the binary system ethane + 2-methylpropane was determined from the critical temperature of ethane up to the critical temperature of 2-methylpropane. The results are compared with vapor-liquid equilibrium data reported earlier on this system and with the critical curve that Is predicted for this system from the Peng-Roblnson equation of state.

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Cited by 108 publications
(72 citation statements)
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“…This apparatus was already described for the first time in 1878 [39] and is still one of the most accurate equipment for measuring phase equilibria. A schematic drawing of the apparatus can be found elsewhere [40]. The Cailletet equipment allows measurement of phase equilibria within a pressure range of 0.1-15 MPa and temperatures from 255 to 470 K, depending on the heat-transferring fluid used.…”
Section: Methodsmentioning
confidence: 99%
“…This apparatus was already described for the first time in 1878 [39] and is still one of the most accurate equipment for measuring phase equilibria. A schematic drawing of the apparatus can be found elsewhere [40]. The Cailletet equipment allows measurement of phase equilibria within a pressure range of 0.1-15 MPa and temperatures from 255 to 470 K, depending on the heat-transferring fluid used.…”
Section: Methodsmentioning
confidence: 99%
“…A Cailletet apparatus (11) was used to measure bubble pressures of mixtures with xq0.922 and to determine directly the coordinates of the three-phase curves s C20 lg for pressures below 16 MPa. Essentially, this equipment consisted of a half-open glass tube containing the sample.…”
Section: Methodsmentioning
confidence: 99%
“…A detailed description of the experimental set-up can be found in Ref. [18]. The equipment allows access to temperatures of up to 508 K and pressures of up to 15 MPa.…”
Section: Bubble-point Pressure Measurementsmentioning
confidence: 99%