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Desolventizing of Jatropha curcas oil from azeotropes of solvents using ceramic membranes.
Carniel, Naira; Zabot, Giovani L; Paliga, Marshall; Mignoni, Marcelo L; Mazutti, Marcio A; Priamo, Wagner L; Oliveira, J V; Di Luccio, Marco; Tres, Marcus V.
Afiliación
  • Carniel N; a Department of Food Engineering , URI Erechim , Erechim , Brazil.
  • Zabot GL; b Laboratory of Bioresources Engineering , Federal University of Santa Maria, UFSM , Cachoeira do Sul , Brazil.
  • Paliga M; a Department of Food Engineering , URI Erechim , Erechim , Brazil.
  • Mignoni ML; a Department of Food Engineering , URI Erechim , Erechim , Brazil.
  • Mazutti MA; c Department of Chemical Engineering , UFSM , Santa Maria , Brazil.
  • Priamo WL; d Department of Food Technology , IFRS , Sertão , Brazil.
  • Oliveira JV; e Department of Chemical and Food Engineering , UFSC , Florianópolis , Brazil.
  • Di Luccio M; e Department of Chemical and Food Engineering , UFSC , Florianópolis , Brazil.
  • Tres MV; b Laboratory of Bioresources Engineering , Federal University of Santa Maria, UFSM , Cachoeira do Sul , Brazil.
Environ Technol ; 38(23): 2928-2938, 2017 Dec.
Article en En | MEDLINE | ID: mdl-28088876
The separation of Jatropha curcas oil from azeotropes of ethyl alcohol-n-hexane and isopropyl alcohol-n-hexane using ceramic membranes with different cutoffs (5, 10 and 20 kDa) is presented. The mass ratios of oil:azeotropes (O:S) studied were 1:3 for feeding pressures of 0.1, 0.2 and 0.3 MPa, and 1:1 for the feeding pressure of 0.1 MPa. Isopropyl alcohol was the best solvent for the membranes conditioning to permeate n-hexane (240 kg/m2 h). In the separation of J. curcas oil and azeotropes of solvents, both membranes showed oil retention and total flux decreases with time. Overall, the lowest decrease in the retentions was reached in the 5 kDa membrane, while the lowest decrease in the total flux was reached in the 20 kDa. In the separation of oil and ethyl alcohol-n-hexane azeotrope, the best retention at 60 min of the process was equal to 17.3 wt% in the 20 kDa membrane at 0.3 MPa and O:S ratio equalled to 1:3. In this condition, the total permeate flux was 17.5 kg/m2 h. Different retentions and permeabilities are provided when changing the O:S ratio, the feeding pressure and the molecular weight cutoff of membranes.
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Texto completo: 1 Colección: 01-internacional Base de datos: MEDLINE Asunto principal: Solventes / Aceites de Plantas / Cerámica / Jatropha / Fraccionamiento Químico Idioma: En Revista: Environ Technol Asunto de la revista: SAUDE AMBIENTAL / TOXICOLOGIA Año: 2017 Tipo del documento: Article País de afiliación: Brasil Pais de publicación: Reino Unido

Texto completo: 1 Colección: 01-internacional Base de datos: MEDLINE Asunto principal: Solventes / Aceites de Plantas / Cerámica / Jatropha / Fraccionamiento Químico Idioma: En Revista: Environ Technol Asunto de la revista: SAUDE AMBIENTAL / TOXICOLOGIA Año: 2017 Tipo del documento: Article País de afiliación: Brasil Pais de publicación: Reino Unido