Ethanol production from xylose by pichia stipitis NRRL Y-7124 in a stirred tank bioreactor
Main Author: | |
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Publication Date: | 2011 |
Other Authors: | , , |
Format: | Article |
Language: | eng |
Source: | Repositórios Científicos de Acesso Aberto de Portugal (RCAAP) |
Download full: | http://hdl.handle.net/1822/16667 |
Summary: | The ethanol production by Pichia stipitis was evaluated in a stirred tank bioreactor using semidefined medium containing xylose (90.0 g/l) as the main carbon source. Experimental assays were performed according to a 22 full factorial design to evaluate the influence of aeration (0.25 to 0.75 vvm) and agitation (150 to 250 rpm) conditions on ethanol production. In the studied range of values, the agitation increase and aeration decrease favored ethanol production, which was maximum (26.7 g/l) using 250 rpm and 0.25 vvm, conditions that gave a volumetric oxygen transfer coefficient (kLa value) of 4.9 h-1. Under these conditions, the ethanol yield factor, ethanol productivity, and the process efficiency were 0.32 g/g, 0.32 g/l.h, and 63%, respectively. These results are promising and contribute to the development of a suitable process for ethanol production from xylose by Pichia stipitis. |
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Ethanol production from xylose by pichia stipitis NRRL Y-7124 in a stirred tank bioreactorEthanolPichia stipitisXyloseStirred tank bioreactorVolumetric oxygen transfer coefficientScience & TechnologyThe ethanol production by Pichia stipitis was evaluated in a stirred tank bioreactor using semidefined medium containing xylose (90.0 g/l) as the main carbon source. Experimental assays were performed according to a 22 full factorial design to evaluate the influence of aeration (0.25 to 0.75 vvm) and agitation (150 to 250 rpm) conditions on ethanol production. In the studied range of values, the agitation increase and aeration decrease favored ethanol production, which was maximum (26.7 g/l) using 250 rpm and 0.25 vvm, conditions that gave a volumetric oxygen transfer coefficient (kLa value) of 4.9 h-1. Under these conditions, the ethanol yield factor, ethanol productivity, and the process efficiency were 0.32 g/g, 0.32 g/l.h, and 63%, respectively. These results are promising and contribute to the development of a suitable process for ethanol production from xylose by Pichia stipitis.The authors gratefully acknowledge Santander, Fapesp, Capes, and CNPq (Brazil).Associação Brasileira de Engenharia Química (ABEQ)Universidade do MinhoSilva, J. P. A.Mussatto, Solange I.Roberto, Inês ConceiçãoTeixeira, J. A.20112011-01-01T00:00:00Zinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleapplication/pdfhttp://hdl.handle.net/1822/16667eng0104-663210.1590/S0104-66322011000100016info:eu-repo/semantics/openAccessreponame:Repositórios Científicos de Acesso Aberto de Portugal (RCAAP)instname:FCCN, serviços digitais da FCT – Fundação para a Ciência e a Tecnologiainstacron:RCAAP2024-05-11T06:54:19Zoai:repositorium.sdum.uminho.pt:1822/16667Portal AgregadorONGhttps://www.rcaap.pt/oai/openaireinfo@rcaap.ptopendoar:https://opendoar.ac.uk/repository/71602025-05-28T16:08:26.741244Repositórios Científicos de Acesso Aberto de Portugal (RCAAP) - FCCN, serviços digitais da FCT – Fundação para a Ciência e a Tecnologiafalse |
dc.title.none.fl_str_mv |
Ethanol production from xylose by pichia stipitis NRRL Y-7124 in a stirred tank bioreactor |
title |
Ethanol production from xylose by pichia stipitis NRRL Y-7124 in a stirred tank bioreactor |
spellingShingle |
Ethanol production from xylose by pichia stipitis NRRL Y-7124 in a stirred tank bioreactor Silva, J. P. A. Ethanol Pichia stipitis Xylose Stirred tank bioreactor Volumetric oxygen transfer coefficient Science & Technology |
title_short |
Ethanol production from xylose by pichia stipitis NRRL Y-7124 in a stirred tank bioreactor |
title_full |
Ethanol production from xylose by pichia stipitis NRRL Y-7124 in a stirred tank bioreactor |
title_fullStr |
Ethanol production from xylose by pichia stipitis NRRL Y-7124 in a stirred tank bioreactor |
title_full_unstemmed |
Ethanol production from xylose by pichia stipitis NRRL Y-7124 in a stirred tank bioreactor |
title_sort |
Ethanol production from xylose by pichia stipitis NRRL Y-7124 in a stirred tank bioreactor |
author |
Silva, J. P. A. |
author_facet |
Silva, J. P. A. Mussatto, Solange I. Roberto, Inês Conceição Teixeira, J. A. |
author_role |
author |
author2 |
Mussatto, Solange I. Roberto, Inês Conceição Teixeira, J. A. |
author2_role |
author author author |
dc.contributor.none.fl_str_mv |
Universidade do Minho |
dc.contributor.author.fl_str_mv |
Silva, J. P. A. Mussatto, Solange I. Roberto, Inês Conceição Teixeira, J. A. |
dc.subject.por.fl_str_mv |
Ethanol Pichia stipitis Xylose Stirred tank bioreactor Volumetric oxygen transfer coefficient Science & Technology |
topic |
Ethanol Pichia stipitis Xylose Stirred tank bioreactor Volumetric oxygen transfer coefficient Science & Technology |
description |
The ethanol production by Pichia stipitis was evaluated in a stirred tank bioreactor using semidefined medium containing xylose (90.0 g/l) as the main carbon source. Experimental assays were performed according to a 22 full factorial design to evaluate the influence of aeration (0.25 to 0.75 vvm) and agitation (150 to 250 rpm) conditions on ethanol production. In the studied range of values, the agitation increase and aeration decrease favored ethanol production, which was maximum (26.7 g/l) using 250 rpm and 0.25 vvm, conditions that gave a volumetric oxygen transfer coefficient (kLa value) of 4.9 h-1. Under these conditions, the ethanol yield factor, ethanol productivity, and the process efficiency were 0.32 g/g, 0.32 g/l.h, and 63%, respectively. These results are promising and contribute to the development of a suitable process for ethanol production from xylose by Pichia stipitis. |
publishDate |
2011 |
dc.date.none.fl_str_mv |
2011 2011-01-01T00:00:00Z |
dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/article |
format |
article |
status_str |
publishedVersion |
dc.identifier.uri.fl_str_mv |
http://hdl.handle.net/1822/16667 |
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http://hdl.handle.net/1822/16667 |
dc.language.iso.fl_str_mv |
eng |
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eng |
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0104-6632 10.1590/S0104-66322011000100016 |
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openAccess |
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application/pdf |
dc.publisher.none.fl_str_mv |
Associação Brasileira de Engenharia Química (ABEQ) |
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Associação Brasileira de Engenharia Química (ABEQ) |
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