dc.creatorMafra, MR
dc.creatorKrahenbuhl, MA
dc.date2006
dc.dateMAR-APR
dc.date2014-11-14T06:44:37Z
dc.date2015-11-26T17:13:40Z
dc.date2014-11-14T06:44:37Z
dc.date2015-11-26T17:13:40Z
dc.date.accessioned2018-03-29T00:02:01Z
dc.date.available2018-03-29T00:02:01Z
dc.identifierJournal Of Chemical And Engineering Data. Amer Chemical Soc, v. 51, n. 2, n. 753, n. 756, 2006.
dc.identifier0021-9568
dc.identifierWOS:000236005000081
dc.identifier10.1021/je050500d
dc.identifierhttp://www.repositorio.unicamp.br/jspui/handle/REPOSIP/81268
dc.identifierhttp://www.repositorio.unicamp.br/handle/REPOSIP/81268
dc.identifierhttp://repositorio.unicamp.br/jspui/handle/REPOSIP/81268
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/1281624
dc.descriptionWe measured the liquid-liquid equilibrium and obtained the tie lines for the ternary systems of (water + acetone) and either cumene or alpha-methylstyrene or phenol at two temperatures of (323.15 and 333.15) K, at a pressure of 0.1 MPa. The NRTL model and the UNIQUAC model were fit to the experimental results in order to obtain interaction parameters for the components. The standard deviations of the calculated values from the experimental results were in the range (0.0026 to 0.0081). The UNIFAC model, based on group contribution, was also employed to describe the equilibrium conditions. For this model, the standard deviations were in the range (0.015 to 0.079) for these mixtures.
dc.description51
dc.description2
dc.description753
dc.description756
dc.languageen
dc.publisherAmer Chemical Soc
dc.publisherWashington
dc.publisherEUA
dc.relationJournal Of Chemical And Engineering Data
dc.relationJ. Chem. Eng. Data
dc.rightsfechado
dc.sourceWeb of Science
dc.subjectMixtures
dc.subjectSystems
dc.titleLiquid-liquid equilibrium of (water plus acetone) with cumene or alpha-methylstyrene or phenol at temperatures of (323.15 and 333.15) K
dc.typeArtículos de revistas


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