Transesterification of sunflower oil produced by solvent extraction
dc.contributor.author | Maristhela Passoni de Araújo Marin | |
dc.contributor.author | Luis Novazzi | |
dc.contributor.author | DENARI, M. L. | |
dc.contributor.authorOrcid | https://orcid.org/0000-0003-1516-2937 | |
dc.contributor.authorOrcid | https://orcid.org/0000-0002-2234-7182 | |
dc.date.accessioned | 2023-08-26T23:48:39Z | |
dc.date.available | 2023-08-26T23:48:39Z | |
dc.date.issued | 2014-11-16 | |
dc.description.abstract | In this work, the leaching of oil from sunflower seeds using hexane was studied. The solution of oil / hexane was thereafter transesterified, with methanol and potassium hydroxide (KOH) as the catalyst, in a batch reactor, for 1 hour and with a constant temperature of 45 °C. It is important to point out that the extracted oil was not refined and was directly used on transesterification reactions. The hexane in the oil / hexane solution acted as a cosolvent and made the oil / methanol mixture forms a single-phase. Experimental results obtained in the transesterification reactions showed that the increase of methanol / oil mole ratio on reaction yield is negative, whereas the increase of catalyst concentration on reaction yield is positive. Reaction yields decreased 18.00% on average when the mole ratio methanol / oil was increased. When catalyst concentration was augmented, reaction yields increased 15.19%, on average. These results are statistically meaningful, since the standard deviation was equal to 0.48%. Moreover, an interaction between methanol / oil mole ratio and catalyst concentration on reaction yield was observed. | |
dc.description.firstpage | 558 | |
dc.description.lastpage | 562 | |
dc.identifier.citation | MARIN, M. P. A.; NOVAZZI, L.; DENARI, M. L. Transesterification of sunflower oil produced by solvent extraction. Sustainable Engineering Forum 2014 - Core Programming Area at the 2014 AIChE Annual Meeting, p. 558-562, nov. 2014. | |
dc.identifier.uri | https://repositorio.fei.edu.br/handle/FEI/4924 | |
dc.relation.ispartof | Sustainable Engineering Forum 2014 - Core Programming Area at the 2014 AIChE Annual Meeting | |
dc.rights | Acesso Restrito | |
dc.subject.otherlanguage | Biodiesel | |
dc.subject.otherlanguage | Solvent extraction | |
dc.subject.otherlanguage | Sunflower | |
dc.subject.otherlanguage | Transesterification | |
dc.title | Transesterification of sunflower oil produced by solvent extraction | |
dc.type | Artigo de evento | |
fei.scopus.citations | 0 | |
fei.scopus.eid | 2-s2.0-84958581888 | |
fei.scopus.subject | Catalyst concentration | |
fei.scopus.subject | Constant temperature | |
fei.scopus.subject | Hexane solutions | |
fei.scopus.subject | Methanol mixtures | |
fei.scopus.subject | Reaction yields | |
fei.scopus.subject | Standard deviation | |
fei.scopus.subject | Sunflower | |
fei.scopus.subject | Transesterification reaction | |
fei.scopus.updated | 2024-12-01 | |
fei.scopus.url | https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=84958581888&origin=inward |