2014-10-202014-10-201997-12MACHADO, Nélio T.; BRUNNER, Gerd. High pressure vapor-liquid equilibria of palm fatty acids distillates-carbon dioxide system. Ciência e Tecnologia de Alimentos, Campinas, v. 17, n. 4, p. 354-360, dez. 1997. Disponível em: <http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0101-20611997000400003&lng=pt&nrm=iso>. Acesso em: 30 jun. 2014. <http://dx.doi.org/10.1590/S0101-20611997000400003>.1678-457Xhttps://repositorio.ufpa.br/handle/2011/5891Vapor-Liquid equilibria of palm fatty acids distillates/carbon dioxide system has been investigated experimentally at temperatures of 333, 353, and 373 K and pressures of 20, 23, 26, and 29 MPa using the static method. Experimental data for the quasi-binary system palm fatty acids distillates/carbon dioxide has been correlated with Redlich-Kwong-Aspen equation of state. Modeling shows good agreement with experimental data. Selectivity obtained indicates that supercritical carbon dioxide is a reasonable solvent for separating saturated (palmitic acid) and unsaturated (oleic+linoleic acids) fatty acids from palm fatty acids distillates in a continuous multistage countercurrent column.engAcesso AbertoTermodinâmicaEquilíbrio químicoEquilíbrio líquido-vaporExtração por solventesExtração com fluído supercríticoExtração com CO2Ácidos graxosDióxido de carbonoArtigo de Periódico