Performance of an enzymatic packed bed reactor running on babassu oil to yield fatty ethyl esters (FAEE) in a solvent-free system

The transesterification reaction of babassu oil with ethanol mediated by Burkholderia cepacia lipase immobilized on SiO2-PVA composite was assessed in a packed bed reactor running in the continuous mode. Experiments were performed in a solvent-free system at 50 °C. The performance of the reactor (14...

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Main Authors: Aline Simões, Lucas Ramos, Larissa Freitas, Julio Santos, Gisella Zanin, Heizir de Castro
Format: Article
Language:English
Published: Green Wave Publishing of Canada 2015-06-01
Series:Biofuel Research Journal
Subjects:
Online Access:http://www.biofueljournal.com/pdf_9622_b1e46f782df5f50b709dfe6b889a70d8.html
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spelling doaj-2bd5c28f809c476aa9c64a63de8edc572020-11-24T22:56:48ZengGreen Wave Publishing of CanadaBiofuel Research Journal2292-87822292-87822015-06-01222422479622Performance of an enzymatic packed bed reactor running on babassu oil to yield fatty ethyl esters (FAEE) in a solvent-free systemAline Simões0Lucas Ramos1Larissa Freitas2Julio Santos3Gisella Zanin4Heizir de Castro5Engineering School of Lorena, University of São Paulo Estrada Municipal do Campinho s/n, 12602-810 Lorena, São Paulo, Brazil.Engineering School of Lorena, University of São Paulo Estrada Municipal do Campinho s/n, 12602-810 Lorena, São Paulo, Brazil.Engineering School of Lorena, University of São Paulo Estrada Municipal do Campinho s/n, 12602-810 Lorena, São Paulo, Brazil.Engineering School of Lorena, University of São Paulo Estrada Municipal do Campinho s/n, 12602-810 Lorena, São Paulo, Brazil.State University of Maringa, Department of Chemical Engineering, Av. Colombo 5790, E-46, 87020-900, Maringa – PR, Brazil.State University of Maringa, Department of Chemical Engineering, Av. Colombo 5790, E-46, 87020-900, Maringa – PR, Brazil.The transesterification reaction of babassu oil with ethanol mediated by Burkholderia cepacia lipase immobilized on SiO2-PVA composite was assessed in a packed bed reactor running in the continuous mode. Experiments were performed in a solvent-free system at 50 °C. The performance of the reactor (14 mm ×210 mm) was evaluated using babassu oil and ethanol at two molar ratios of 1:7 and 1:12, respectively, and operational limits in terms of substrate flow rate were determined. The system’s performance was quantified for different flow rates corresponding to space times between 7 and 13 h. Under each condition, the impact of the space time on the ethyl esters formation, the transesterification yield and productivity were determined. The oil to ethanol molar ratio was found as a critical parameter in the conversion of babassu oil into the correspondent ethyl esters. The highest transesterification yield of 96.0 ± 0.9% and productivity of 41.1 ± 1.6 mgester gcatalyst-1h-1 were achieved at the oil to ethanol molar ratio of 1:12 and for space times equal or higher than 11 h. Moreover, the immobilized lipase was found stable with respect to its catalytic characteristics, exhibiting a half-life of 32 d.http://www.biofueljournal.com/pdf_9622_b1e46f782df5f50b709dfe6b889a70d8.htmlBiodieselTransesterificationBabassu oilPacked bed reactorImmobilized lipaseContinuous mode
collection DOAJ
language English
format Article
sources DOAJ
author Aline Simões
Lucas Ramos
Larissa Freitas
Julio Santos
Gisella Zanin
Heizir de Castro
spellingShingle Aline Simões
Lucas Ramos
Larissa Freitas
Julio Santos
Gisella Zanin
Heizir de Castro
Performance of an enzymatic packed bed reactor running on babassu oil to yield fatty ethyl esters (FAEE) in a solvent-free system
Biofuel Research Journal
Biodiesel
Transesterification
Babassu oil
Packed bed reactor
Immobilized lipase
Continuous mode
author_facet Aline Simões
Lucas Ramos
Larissa Freitas
Julio Santos
Gisella Zanin
Heizir de Castro
author_sort Aline Simões
title Performance of an enzymatic packed bed reactor running on babassu oil to yield fatty ethyl esters (FAEE) in a solvent-free system
title_short Performance of an enzymatic packed bed reactor running on babassu oil to yield fatty ethyl esters (FAEE) in a solvent-free system
title_full Performance of an enzymatic packed bed reactor running on babassu oil to yield fatty ethyl esters (FAEE) in a solvent-free system
title_fullStr Performance of an enzymatic packed bed reactor running on babassu oil to yield fatty ethyl esters (FAEE) in a solvent-free system
title_full_unstemmed Performance of an enzymatic packed bed reactor running on babassu oil to yield fatty ethyl esters (FAEE) in a solvent-free system
title_sort performance of an enzymatic packed bed reactor running on babassu oil to yield fatty ethyl esters (faee) in a solvent-free system
publisher Green Wave Publishing of Canada
series Biofuel Research Journal
issn 2292-8782
2292-8782
publishDate 2015-06-01
description The transesterification reaction of babassu oil with ethanol mediated by Burkholderia cepacia lipase immobilized on SiO2-PVA composite was assessed in a packed bed reactor running in the continuous mode. Experiments were performed in a solvent-free system at 50 °C. The performance of the reactor (14 mm ×210 mm) was evaluated using babassu oil and ethanol at two molar ratios of 1:7 and 1:12, respectively, and operational limits in terms of substrate flow rate were determined. The system’s performance was quantified for different flow rates corresponding to space times between 7 and 13 h. Under each condition, the impact of the space time on the ethyl esters formation, the transesterification yield and productivity were determined. The oil to ethanol molar ratio was found as a critical parameter in the conversion of babassu oil into the correspondent ethyl esters. The highest transesterification yield of 96.0 ± 0.9% and productivity of 41.1 ± 1.6 mgester gcatalyst-1h-1 were achieved at the oil to ethanol molar ratio of 1:12 and for space times equal or higher than 11 h. Moreover, the immobilized lipase was found stable with respect to its catalytic characteristics, exhibiting a half-life of 32 d.
topic Biodiesel
Transesterification
Babassu oil
Packed bed reactor
Immobilized lipase
Continuous mode
url http://www.biofueljournal.com/pdf_9622_b1e46f782df5f50b709dfe6b889a70d8.html
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