Ethanol production from xylose by Pichia stipitis NRRL Y-7124 in a stirred tank bioreactor
Autor(a) principal: | |
---|---|
Data de Publicação: | 2011 |
Outros Autores: | , , |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | Brazilian Journal of Chemical Engineering |
Texto Completo: | http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322011000100016 |
Resumo: | The ethanol production by Pichia stipitis was evaluated in a stirred tank bioreactor using semi-defined 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. |
id |
ABEQ-1_c0ca7210ba3950556fe4c3a183d57f91 |
---|---|
oai_identifier_str |
oai:scielo:S0104-66322011000100016 |
network_acronym_str |
ABEQ-1 |
network_name_str |
Brazilian Journal of Chemical Engineering |
repository_id_str |
|
spelling |
Ethanol production from xylose by Pichia stipitis NRRL Y-7124 in a stirred tank bioreactorEthanolPichia stipitisXyloseStirred tank bioreactorVolumetric oxygen transfer coefficientThe ethanol production by Pichia stipitis was evaluated in a stirred tank bioreactor using semi-defined 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.Brazilian Society of Chemical Engineering2011-03-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322011000100016Brazilian Journal of Chemical Engineering v.28 n.1 2011reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/S0104-66322011000100016info:eu-repo/semantics/openAccessSilva,J. P. A.Mussatto,S. I.Roberto,I. C.Teixeira,J. A.eng2011-03-15T00:00:00Zoai:scielo:S0104-66322011000100016Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:2011-03-15T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false |
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 |
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,S. I. Roberto,I. C. Teixeira,J. A. |
author_role |
author |
author2 |
Mussatto,S. I. Roberto,I. C. Teixeira,J. A. |
author2_role |
author author author |
dc.contributor.author.fl_str_mv |
Silva,J. P. A. Mussatto,S. I. Roberto,I. C. Teixeira,J. A. |
dc.subject.por.fl_str_mv |
Ethanol Pichia stipitis Xylose Stirred tank bioreactor Volumetric oxygen transfer coefficient |
topic |
Ethanol Pichia stipitis Xylose Stirred tank bioreactor Volumetric oxygen transfer coefficient |
description |
The ethanol production by Pichia stipitis was evaluated in a stirred tank bioreactor using semi-defined 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 |
2011-03-01 |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/article |
dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
format |
article |
status_str |
publishedVersion |
dc.identifier.uri.fl_str_mv |
http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322011000100016 |
url |
http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322011000100016 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
10.1590/S0104-66322011000100016 |
dc.rights.driver.fl_str_mv |
info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
text/html |
dc.publisher.none.fl_str_mv |
Brazilian Society of Chemical Engineering |
publisher.none.fl_str_mv |
Brazilian Society of Chemical Engineering |
dc.source.none.fl_str_mv |
Brazilian Journal of Chemical Engineering v.28 n.1 2011 reponame:Brazilian Journal of Chemical Engineering instname:Associação Brasileira de Engenharia Química (ABEQ) instacron:ABEQ |
instname_str |
Associação Brasileira de Engenharia Química (ABEQ) |
instacron_str |
ABEQ |
institution |
ABEQ |
reponame_str |
Brazilian Journal of Chemical Engineering |
collection |
Brazilian Journal of Chemical Engineering |
repository.name.fl_str_mv |
Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ) |
repository.mail.fl_str_mv |
rgiudici@usp.br||rgiudici@usp.br |
_version_ |
1754213173433466880 |