dc.creatorMunoz, LAL
dc.creatorKrahenbuhl, MA
dc.date2001
dc.dateJAN-FEB
dc.date2014-11-20T00:52:54Z
dc.date2015-11-26T16:01:44Z
dc.date2014-11-20T00:52:54Z
dc.date2015-11-26T16:01:44Z
dc.date.accessioned2018-03-28T22:51:15Z
dc.date.available2018-03-28T22:51:15Z
dc.identifierJournal Of Chemical And Engineering Data. Amer Chemical Soc, v. 46, n. 1, n. 120, n. 124, 2001.
dc.identifier0021-9568
dc.identifierWOS:000166498100021
dc.identifier10.1021/je000033u
dc.identifierhttp://www.repositorio.unicamp.br/jspui/handle/REPOSIP/60785
dc.identifierhttp://www.repositorio.unicamp.br/handle/REPOSIP/60785
dc.identifierhttp://repositorio.unicamp.br/jspui/handle/REPOSIP/60785
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/1264912
dc.descriptionVapor liquid equilibria (VLE) of the binary systems n-butanal + butyric acid and n-butanol + acetic acid were determined at two pressures, 26.65 and 53.33 kPa. The equipment used was a flow ebulliometer, which is ideal for reactive systems . The quality of the measured P-T-x-y data was verified by applying the thermodynamic consistency test of Van Ness and Fredenslund. The binary interaction parameters for the determination of the liquid-phase activity coefficients, represented by the models Wilson, UNIQUAC, and NRTL, were adjusted by using the maximum likelihood method. The nonideality of the vapor phase was considered by using a chemical theory with the correlation of Hayden and O'Connell for the calculation of the second virial coefficient and the prediction of the chemical equilibrium dimerization constant.
dc.description46
dc.description1
dc.description120
dc.description124
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.titleIsobaric vapor liquid equilibrium (VLE) data of the systems n-butanol plus butyric acid and n-butanol plus acetic acid
dc.typeArtículos de revistas


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