Vapor-liquid equilibrium for the system hydrogen—benzene—cyclohexane— n -hexane
dc.contributor.author | Brainard, Alan J. | en_US |
dc.contributor.author | Williams, Brymer | en_US |
dc.date.accessioned | 2006-04-28T15:42:47Z | |
dc.date.available | 2006-04-28T15:42:47Z | |
dc.date.issued | 1967-01 | en_US |
dc.identifier.citation | Brainard, Alan J.; Williams, Brymer (1967)."Vapor-liquid equilibrium for the system hydrogen—benzene—cyclohexane— n -hexane." AIChE Journal 13(1): 60-69. <http://hdl.handle.net/2027.42/37345> | en_US |
dc.identifier.issn | 0001-1541 | en_US |
dc.identifier.issn | 1547-5905 | en_US |
dc.identifier.uri | https://hdl.handle.net/2027.42/37345 | |
dc.description.abstract | This paper presents vapor-liquid equilibrium data for the system hydrogen—benzene—cyclohexane— n -hexane over the pressure range of 500 to 2,000 lb./sq.in.abs. and the temperature range of 200° to 300°F. Experimental equipment was constructed that was capable of operating at pressures of 3,000 lb./sq.in.abs. and at temperatures of 400°F. A static equilibrium cell, which had a sample port for both the liquid and vapor phases, was employed. Separation of the hydrogen from the hydrocarbons by means of a liquid nitrogen cold trap was utilized before performing the hydrocarbon analyses on a mass spectrometer. Three hydrocarbon mixtures were charged to the equilibrium cell, and for each charge, isotherms of 200°, 250°, and 300°F. were run for equilibrium pressures of 500, 1,000, 1,500 and 2,000 lb./sq.in.abs. These thirty-six quaternary equilibrium runs resulted in a total of one hundred and forty-four equilibrium data points. In addition, four binary equilibrium runs were determined both for the hydrogen-benzene and hydrogen-cyclohexane systems. A modified version of the Chao-Seader correlation was used to predict the data. This correlation was able to predict all the quaternary equilibrium ratios with an average deviation of 4.86%. | en_US |
dc.format.extent | 1401860 bytes | |
dc.format.extent | 3118 bytes | |
dc.format.mimetype | application/pdf | |
dc.format.mimetype | text/plain | |
dc.language.iso | en_US | |
dc.publisher | American Institute of Chemical Engineers | en_US |
dc.publisher | Wiley Periodiocals, Inc. | en_US |
dc.subject.other | Chemistry | en_US |
dc.subject.other | Chemical Engineering | en_US |
dc.title | Vapor-liquid equilibrium for the system hydrogen—benzene—cyclohexane— n -hexane | en_US |
dc.type | Article | en_US |
dc.rights.robots | IndexNoFollow | en_US |
dc.subject.hlbsecondlevel | Chemical Engineering | en_US |
dc.subject.hlbtoplevel | Engineering | en_US |
dc.subject.hlbtoplevel | Science | en_US |
dc.description.peerreviewed | Peer Reviewed | en_US |
dc.contributor.affiliationum | University of Michigan, Ann Arbor, Michigan | en_US |
dc.contributor.affiliationum | University of Michigan, Ann Arbor, Michigan | en_US |
dc.description.bitstreamurl | http://deepblue.lib.umich.edu/bitstream/2027.42/37345/1/690130113_ftp.pdf | en_US |
dc.identifier.doi | http://dx.doi.org/10.1002/aic.690130113 | en_US |
dc.identifier.source | AIChE Journal | en_US |
dc.owningcollname | Interdisciplinary and Peer-Reviewed |
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