Use of Candida rugosa lipase immobilized on sepabeads for the amyl caprylate synthesis: Batch and fluidized bed reactor study

Lipase from Candida rugosa was covalently immobilized on Sepabeads EC-EP for application for amyl caprylate synthesis in an organic solvent system. Several solvents were tested in terms of biocatalyst stability and the best result was obtained with isooctane. The lipase-catalyzed esterification in t...

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Autores principales: Saponji,Svetlana, Kneevi-Jugovi,Zorica D, Bezbradica,Dejan I, Zuza,Milena G, Saied,Omar Ali, Boskovi-Vragolovi,Nevenka, Mijin,Dusan Z
Lenguaje:English
Publicado: Pontificia Universidad Católica de Valparaíso 2010
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Acceso en línea:http://www.scielo.cl/scielo.php?script=sci_arttext&pid=S0717-34582010000600012
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spelling oai:scielo:S0717-345820100006000122011-05-26Use of Candida rugosa lipase immobilized on sepabeads for the amyl caprylate synthesis: Batch and fluidized bed reactor studySaponji,SvetlanaKneevi-Jugovi,Zorica DBezbradica,Dejan IZuza,Milena GSaied,Omar AliBoskovi-Vragolovi,NevenkaMijin,Dusan Z bioreactors covalent immobilization ester non-aqueous system optimization technique Lipase from Candida rugosa was covalently immobilized on Sepabeads EC-EP for application for amyl caprylate synthesis in an organic solvent system. Several solvents were tested in terms of biocatalyst stability and the best result was obtained with isooctane. The lipase-catalyzed esterification in the selected system was performed in batch and fluidized bed reactor systems. The influence of several important reaction parameters including temperature, initial water content, enzyme loading, acid/alcohol molar ratio, and time of addition of molecular sieves is carefully analyzed by means of an experimental design. Almost complete conversion (> 99%) of the substrate to ester could be performed in a batch reactor system, using lipase loading as low as 37 mg g-1 dry support and in a relatively short time (24 hrs) at 37�C, when high initial substrate molar ratio of 2.2 is used. Kinetics in a fluidized bed reactor system seems to still have a slightly better profile than in the batch system (90.2% yields after 14 hrs). The fluidized bed reactor operated for up 70 hrs almost with no loss in productivity, implying that the proposed process and the immobilized system could provide a promising approach for the amyl caprylate synthesis at the industrial scale.info:eu-repo/semantics/openAccessPontificia Universidad Católica de ValparaísoElectronic Journal of Biotechnology v.13 n.6 20102010-11-01text/htmlhttp://www.scielo.cl/scielo.php?script=sci_arttext&pid=S0717-34582010000600012en
institution Scielo Chile
collection Scielo Chile
language English
topic bioreactors
covalent immobilization
ester
non-aqueous system
optimization technique
spellingShingle bioreactors
covalent immobilization
ester
non-aqueous system
optimization technique
Saponji,Svetlana
Kneevi-Jugovi,Zorica D
Bezbradica,Dejan I
Zuza,Milena G
Saied,Omar Ali
Boskovi-Vragolovi,Nevenka
Mijin,Dusan Z
Use of Candida rugosa lipase immobilized on sepabeads for the amyl caprylate synthesis: Batch and fluidized bed reactor study
description Lipase from Candida rugosa was covalently immobilized on Sepabeads EC-EP for application for amyl caprylate synthesis in an organic solvent system. Several solvents were tested in terms of biocatalyst stability and the best result was obtained with isooctane. The lipase-catalyzed esterification in the selected system was performed in batch and fluidized bed reactor systems. The influence of several important reaction parameters including temperature, initial water content, enzyme loading, acid/alcohol molar ratio, and time of addition of molecular sieves is carefully analyzed by means of an experimental design. Almost complete conversion (> 99%) of the substrate to ester could be performed in a batch reactor system, using lipase loading as low as 37 mg g-1 dry support and in a relatively short time (24 hrs) at 37�C, when high initial substrate molar ratio of 2.2 is used. Kinetics in a fluidized bed reactor system seems to still have a slightly better profile than in the batch system (90.2% yields after 14 hrs). The fluidized bed reactor operated for up 70 hrs almost with no loss in productivity, implying that the proposed process and the immobilized system could provide a promising approach for the amyl caprylate synthesis at the industrial scale.
author Saponji,Svetlana
Kneevi-Jugovi,Zorica D
Bezbradica,Dejan I
Zuza,Milena G
Saied,Omar Ali
Boskovi-Vragolovi,Nevenka
Mijin,Dusan Z
author_facet Saponji,Svetlana
Kneevi-Jugovi,Zorica D
Bezbradica,Dejan I
Zuza,Milena G
Saied,Omar Ali
Boskovi-Vragolovi,Nevenka
Mijin,Dusan Z
author_sort Saponji,Svetlana
title Use of Candida rugosa lipase immobilized on sepabeads for the amyl caprylate synthesis: Batch and fluidized bed reactor study
title_short Use of Candida rugosa lipase immobilized on sepabeads for the amyl caprylate synthesis: Batch and fluidized bed reactor study
title_full Use of Candida rugosa lipase immobilized on sepabeads for the amyl caprylate synthesis: Batch and fluidized bed reactor study
title_fullStr Use of Candida rugosa lipase immobilized on sepabeads for the amyl caprylate synthesis: Batch and fluidized bed reactor study
title_full_unstemmed Use of Candida rugosa lipase immobilized on sepabeads for the amyl caprylate synthesis: Batch and fluidized bed reactor study
title_sort use of candida rugosa lipase immobilized on sepabeads for the amyl caprylate synthesis: batch and fluidized bed reactor study
publisher Pontificia Universidad Católica de Valparaíso
publishDate 2010
url http://www.scielo.cl/scielo.php?script=sci_arttext&pid=S0717-34582010000600012
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