Optimized interesterification of virgin olive oil with a fully hydrogenated fat in a batch reactor: Effect of mass transfer limitations

Abstract The lipase‐catalyzed interesterification of virgin olive oil and fully hydrogenated palm oil (FHPO) was studied in a batch reactor operating at 75 °C. The reactions between olive oil {rich in OOO (32.36%), OPO (21.7%) and OLO (11.6%) [L = linoleic; O = oleic; P = palmitic acid]} and the ful...

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Published in:European Journal of Lipid Science and Technology
Main Authors: Criado, Manuel, Hernández‐Martín, Estela, Otero, Cristina
Format: Article in Journal/Newspaper
Language:English
Published: Wiley 2007
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Online Access:http://dx.doi.org/10.1002/ejlt.200600270
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spelling crwiley:10.1002/ejlt.200600270 2024-06-02T07:58:08+00:00 Optimized interesterification of virgin olive oil with a fully hydrogenated fat in a batch reactor: Effect of mass transfer limitations Criado, Manuel Hernández‐Martín, Estela Otero, Cristina 2007 http://dx.doi.org/10.1002/ejlt.200600270 https://api.wiley.com/onlinelibrary/tdm/v1/articles/10.1002%2Fejlt.200600270 https://onlinelibrary.wiley.com/doi/pdf/10.1002/ejlt.200600270 en eng Wiley http://onlinelibrary.wiley.com/termsAndConditions#vor European Journal of Lipid Science and Technology volume 109, issue 5, page 474-485 ISSN 1438-7697 1438-9312 journal-article 2007 crwiley https://doi.org/10.1002/ejlt.200600270 2024-05-03T11:24:31Z Abstract The lipase‐catalyzed interesterification of virgin olive oil and fully hydrogenated palm oil (FHPO) was studied in a batch reactor operating at 75 °C. The reactions between olive oil {rich in OOO (32.36%), OPO (21.7%) and OLO (11.6%) [L = linoleic; O = oleic; P = palmitic acid]} and the fully hydrogenated fat {(36.5% PSP, 28.8% PPP, 23.2% SPS) [S = stearic acid]} produced semi‐solid fats. For an initial weight ratio of olive oil to FHPO of 60 : 40, the reaction product is a complex mixture of triacylglycerol (TAG) species. The TAG profile of the fat product is time dependent. Because of the high viscosity of the liquid reagent phase, it was important to determine if mass transfer effects were significant. Hence, the reaction was optimized with respect to the type and speed of agitation employed, temperature, use of solvent, and the type of biocatalyst. Three immobilized lipases [from Thermomyces lanuginosus (TL IM), Rhizomucor miehei (RM IM) and Candida antarctica B (Novozym 435)] were compared as catalysts for the interesterification reaction. Equilibrium is reached four times faster (in 1–4 h) with a magnetic stirrer to provide agitation than when agitation is not sufficient, i.e. when orbital agitation is employed. Equilibrium was reached faster with Lipozyme TL IM than with the other two lipases. The effects of all the factors investigated on the composition of the products have also been determined. Semi‐solid fats obtained with the non‐specific Novozym 435 contain levels of unsaturated fatty acid residues on sn ‐2 sites that are similar to the products obtained with the 1(3)‐regiospecific enzymes Lipozyme TL IM and RM IM. The chemical properties of the product semi‐solid fat were characterized. The fat prepared using optimal reaction conditions contained 17.20% OPO, 13.61% OOO, 11.09% POP, and 10.35% OSP isomers as the primary products. The induction time obtained in the assay of the oxidative stability of the fat product was 21 h at 98 °C. The lipases Lipozyme TL IM and Novozym 435 were very ... Article in Journal/Newspaper Antarc* Antarctica Wiley Online Library European Journal of Lipid Science and Technology 109 5 474 485
institution Open Polar
collection Wiley Online Library
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description Abstract The lipase‐catalyzed interesterification of virgin olive oil and fully hydrogenated palm oil (FHPO) was studied in a batch reactor operating at 75 °C. The reactions between olive oil {rich in OOO (32.36%), OPO (21.7%) and OLO (11.6%) [L = linoleic; O = oleic; P = palmitic acid]} and the fully hydrogenated fat {(36.5% PSP, 28.8% PPP, 23.2% SPS) [S = stearic acid]} produced semi‐solid fats. For an initial weight ratio of olive oil to FHPO of 60 : 40, the reaction product is a complex mixture of triacylglycerol (TAG) species. The TAG profile of the fat product is time dependent. Because of the high viscosity of the liquid reagent phase, it was important to determine if mass transfer effects were significant. Hence, the reaction was optimized with respect to the type and speed of agitation employed, temperature, use of solvent, and the type of biocatalyst. Three immobilized lipases [from Thermomyces lanuginosus (TL IM), Rhizomucor miehei (RM IM) and Candida antarctica B (Novozym 435)] were compared as catalysts for the interesterification reaction. Equilibrium is reached four times faster (in 1–4 h) with a magnetic stirrer to provide agitation than when agitation is not sufficient, i.e. when orbital agitation is employed. Equilibrium was reached faster with Lipozyme TL IM than with the other two lipases. The effects of all the factors investigated on the composition of the products have also been determined. Semi‐solid fats obtained with the non‐specific Novozym 435 contain levels of unsaturated fatty acid residues on sn ‐2 sites that are similar to the products obtained with the 1(3)‐regiospecific enzymes Lipozyme TL IM and RM IM. The chemical properties of the product semi‐solid fat were characterized. The fat prepared using optimal reaction conditions contained 17.20% OPO, 13.61% OOO, 11.09% POP, and 10.35% OSP isomers as the primary products. The induction time obtained in the assay of the oxidative stability of the fat product was 21 h at 98 °C. The lipases Lipozyme TL IM and Novozym 435 were very ...
format Article in Journal/Newspaper
author Criado, Manuel
Hernández‐Martín, Estela
Otero, Cristina
spellingShingle Criado, Manuel
Hernández‐Martín, Estela
Otero, Cristina
Optimized interesterification of virgin olive oil with a fully hydrogenated fat in a batch reactor: Effect of mass transfer limitations
author_facet Criado, Manuel
Hernández‐Martín, Estela
Otero, Cristina
author_sort Criado, Manuel
title Optimized interesterification of virgin olive oil with a fully hydrogenated fat in a batch reactor: Effect of mass transfer limitations
title_short Optimized interesterification of virgin olive oil with a fully hydrogenated fat in a batch reactor: Effect of mass transfer limitations
title_full Optimized interesterification of virgin olive oil with a fully hydrogenated fat in a batch reactor: Effect of mass transfer limitations
title_fullStr Optimized interesterification of virgin olive oil with a fully hydrogenated fat in a batch reactor: Effect of mass transfer limitations
title_full_unstemmed Optimized interesterification of virgin olive oil with a fully hydrogenated fat in a batch reactor: Effect of mass transfer limitations
title_sort optimized interesterification of virgin olive oil with a fully hydrogenated fat in a batch reactor: effect of mass transfer limitations
publisher Wiley
publishDate 2007
url http://dx.doi.org/10.1002/ejlt.200600270
https://api.wiley.com/onlinelibrary/tdm/v1/articles/10.1002%2Fejlt.200600270
https://onlinelibrary.wiley.com/doi/pdf/10.1002/ejlt.200600270
genre Antarc*
Antarctica
genre_facet Antarc*
Antarctica
op_source European Journal of Lipid Science and Technology
volume 109, issue 5, page 474-485
ISSN 1438-7697 1438-9312
op_rights http://onlinelibrary.wiley.com/termsAndConditions#vor
op_doi https://doi.org/10.1002/ejlt.200600270
container_title European Journal of Lipid Science and Technology
container_volume 109
container_issue 5
container_start_page 474
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