dc.creator | Munoz, LAL | |
dc.creator | Krahenbuhl, MA | |
dc.date | 2001 | |
dc.date | JAN-FEB | |
dc.date | 2014-11-20T00:52:54Z | |
dc.date | 2015-11-26T16:01:44Z | |
dc.date | 2014-11-20T00:52:54Z | |
dc.date | 2015-11-26T16:01:44Z | |
dc.date.accessioned | 2018-03-28T22:51:15Z | |
dc.date.available | 2018-03-28T22:51:15Z | |
dc.identifier | Journal Of Chemical And Engineering Data. Amer Chemical Soc, v. 46, n. 1, n. 120, n. 124, 2001. | |
dc.identifier | 0021-9568 | |
dc.identifier | WOS:000166498100021 | |
dc.identifier | 10.1021/je000033u | |
dc.identifier | http://www.repositorio.unicamp.br/jspui/handle/REPOSIP/60785 | |
dc.identifier | http://www.repositorio.unicamp.br/handle/REPOSIP/60785 | |
dc.identifier | http://repositorio.unicamp.br/jspui/handle/REPOSIP/60785 | |
dc.identifier.uri | http://repositorioslatinoamericanos.uchile.cl/handle/2250/1264912 | |
dc.description | Vapor 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.description | 46 | |
dc.description | 1 | |
dc.description | 120 | |
dc.description | 124 | |
dc.language | en | |
dc.publisher | Amer Chemical Soc | |
dc.publisher | Washington | |
dc.publisher | EUA | |
dc.relation | Journal Of Chemical And Engineering Data | |
dc.relation | J. Chem. Eng. Data | |
dc.rights | fechado | |
dc.source | Web of Science | |
dc.title | Isobaric vapor liquid equilibrium (VLE) data of the systems n-butanol plus butyric acid and n-butanol plus acetic acid | |
dc.type | Artículos de revistas | |