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dc.contributor.authorGui, X.
dc.contributor.authorWang, Wei
dc.contributor.authorWang, C.
dc.contributor.authorZhang, L.
dc.contributor.authorYun, Z.
dc.contributor.authorTang, Z.
dc.date.accessioned2017-08-24T02:18:20Z
dc.date.available2017-08-24T02:18:20Z
dc.date.created2017-08-23T07:21:51Z
dc.date.issued2014
dc.identifier.citationGui, X. and Wang, W. and Wang, C. and Zhang, L. and Yun, Z. and Tang, Z. 2014. Vapor-liquid phase equilibrium data of CO2 in some physical solvents from 285.19 K to 313.26 K. Journal of Chemical & Engineering Data. 59 (3): pp. 844-849.
dc.identifier.urihttp://hdl.handle.net/20.500.11937/55349
dc.identifier.doi10.1021/je400985u
dc.description.abstract

The solubility of CO 2 in polyethylene glycol dimethyl ether (NHD), octamethyl cyclotetrasiloxane (D4), and diethyl succinate (DS) was determined at the temperature variations from 285.19 K to 313.26 K up to 6 MPa by the constant-volume method. Then, Henry's law constant (H) based on mole fraction was obtained by linear fitting of the vapor-liquid phase equilibrium data, and some thermodynamic properties of solutions were also calculated from the correlation of H. The values of H in NHD, D4, and DS vary from 2.5 MPa to 8 MPa and increase in the following order: DS < D4 < NHD, which is identical to the order of the solvents ability to dissolve CO 2 . Additionally, Henry's law constant increases with temperature increase to confirm the solubility of CO 2 decrease in the corresponding solvents for the pressure range studied. © 2014 American Chemical Society.

dc.publisherAmerican Chemical Society
dc.titleVapor-liquid phase equilibrium data of CO2 in some physical solvents from 285.19 K to 313.26 K
dc.typeJournal Article
dcterms.source.volume59
dcterms.source.number3
dcterms.source.startPage844
dcterms.source.endPage849
dcterms.source.issn0021-9568
dcterms.source.titleJournal of Chemical & Engineering Data
curtin.departmentDepartment of Chemical Engineering
curtin.accessStatusFulltext not available


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