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(Referência obtida automaticamente do Web of Science, por meio da informação sobre o financiamento pela FAPESP e o número do processo correspondente, incluída na publicação pelos autores.)

Liquid-Liquid Equilibrium Data for Systems Containing Vegetable Oils, Anhydrous Ethanol, and Hexane at (313.15, 318.15, and 328.15) K

Texto completo
Autor(es):
Lanza, Marcelo [1] ; Sanaiotti, Guilherme [1] ; Batista, Eduardo A. C. [1] ; Poppi, Ronei J. [1] ; Meirelles, Antonio J. A. [2]
Número total de Autores: 5
Afiliação do(s) autor(es):
[1] Univ Estadual Campinas, Inst Chem, Dept Analyt Chem, Chemometr Lab, BR-13083862 Campinas, SP - Brazil
[2] Univ Estadual Campinas, Dept Food Engn, Lab Extract Appl Thermodynam & Equilibrium, ExTrAE, Fac Food Engn, BR-13083862 Campinas, SP - Brazil
Número total de Afiliações: 2
Tipo de documento: Artigo Científico
Fonte: JOURNAL OF CHEMICAL AND ENGINEERING DATA; v. 54, n. 6, p. 1850-1859, JUN 2009.
Citações Web of Science: 22
Resumo

The aim of this work was to determine liquid-liquid equilibrium data for systems of interest in ethyl ester (biodiesel) production. The following systems were investigated: refined soybean oil + anhydrous ethanol + hexane at (313.15 +/- 0.1) K and (328.25 +/- 0.1) K, refined canola oil + anhydrous ethanol + hexane at (313.25 +/- 0.1) K and (328.15 +/- 0.1) K, and refined palm oil + anhydrous ethanol + hexane at (318.15 +/- 0.1) K and (328.25 +/- 0.1) K. The instrumental technique of near-infrared spectroscopy allied to multivariate calibration (in this work, this union was denominated ``NIR method{''}) was used for quantification of the phase compositions. The NIR method presented an appropriate experimental accuracy for quantifying equilibrium data at higher temperatures. Good reliability of the phase compositions was confirmed from values of global mass balance deviations ranging from (0.06 to 0.16)%. The experimental data were correlated using the NRTL model with an average global deviation of 0.83%. (AU)

Processo FAPESP: 05/53095-2 - Equilíbrio de fases e processos de separação de misturas graxas e aquosas
Beneficiário:Antonio José de Almeida Meirelles
Modalidade de apoio: Auxílio à Pesquisa - Temático
Processo FAPESP: 04/09591-2 - Equilíbrio de fases líquido-líquido dos sistemas reacionais de etanólise e glicerólise
Beneficiário:Marcelo Lanza
Modalidade de apoio: Bolsas no Brasil - Doutorado