A study on clavulanic acid production by Streptomyces clavuligerus in batch, fed-batch and continuous processes
Autor(a) principal: | |
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Data de Publicação: | 2005 |
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=S0104-66322005000400008 |
Resumo: | Clavulanic acid (CA) is a potent inhibitor of beta-lactamases, enzymes that are responsible for the hydrolysis of beta-lactam antibiotics. It is a secondary metabolite produced by the filamentous aerobic bacterium Streptomyces clavuligerus in submerged cultivations. In the present work clavulanic acid production in batch, fed-batch and continuous bioreactors was studied with the objective of increasing productivity. The operating conditions: temperature, aeration and agitation, were the same in all cases, 28º C, 0.5 vvm and 800 rpm, respectively. The CA concentration obtained in the fed-batch culture, 404 mg L-1, was ca twice the value obtained in the batch culture, 194 mg L-1, while 293 mg L-1 was obtained in the continuous culture. The highest productivity was obtained in the continuous cultivation, 10.6 mg L-1 h-1, as compared with 8.8 mg L-1 h-1 in the fed-batch process and 3.5 mg L-1 h-1 in the batch process, suggesting that continuous culture of Streptomyces clavuligerus is a promising strategy for clavulanic acid production. |
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A study on clavulanic acid production by Streptomyces clavuligerus in batch, fed-batch and continuous processesClavulanic acidBioreactorsEnzymesClavulanic acid (CA) is a potent inhibitor of beta-lactamases, enzymes that are responsible for the hydrolysis of beta-lactam antibiotics. It is a secondary metabolite produced by the filamentous aerobic bacterium Streptomyces clavuligerus in submerged cultivations. In the present work clavulanic acid production in batch, fed-batch and continuous bioreactors was studied with the objective of increasing productivity. The operating conditions: temperature, aeration and agitation, were the same in all cases, 28º C, 0.5 vvm and 800 rpm, respectively. The CA concentration obtained in the fed-batch culture, 404 mg L-1, was ca twice the value obtained in the batch culture, 194 mg L-1, while 293 mg L-1 was obtained in the continuous culture. The highest productivity was obtained in the continuous cultivation, 10.6 mg L-1 h-1, as compared with 8.8 mg L-1 h-1 in the fed-batch process and 3.5 mg L-1 h-1 in the batch process, suggesting that continuous culture of Streptomyces clavuligerus is a promising strategy for clavulanic acid production.Brazilian Society of Chemical Engineering2005-12-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322005000400008Brazilian Journal of Chemical Engineering v.22 n.4 2005reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/S0104-66322005000400008info:eu-repo/semantics/openAccessNeto,A. B.Hirata,D. B.Cassiano Filho,L. C. M.Bellão,C.Badino Júnior,A. C.Hokka,C. O.eng2006-01-02T00:00:00Zoai:scielo:S0104-66322005000400008Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:2006-01-02T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false |
dc.title.none.fl_str_mv |
A study on clavulanic acid production by Streptomyces clavuligerus in batch, fed-batch and continuous processes |
title |
A study on clavulanic acid production by Streptomyces clavuligerus in batch, fed-batch and continuous processes |
spellingShingle |
A study on clavulanic acid production by Streptomyces clavuligerus in batch, fed-batch and continuous processes Neto,A. B. Clavulanic acid Bioreactors Enzymes |
title_short |
A study on clavulanic acid production by Streptomyces clavuligerus in batch, fed-batch and continuous processes |
title_full |
A study on clavulanic acid production by Streptomyces clavuligerus in batch, fed-batch and continuous processes |
title_fullStr |
A study on clavulanic acid production by Streptomyces clavuligerus in batch, fed-batch and continuous processes |
title_full_unstemmed |
A study on clavulanic acid production by Streptomyces clavuligerus in batch, fed-batch and continuous processes |
title_sort |
A study on clavulanic acid production by Streptomyces clavuligerus in batch, fed-batch and continuous processes |
author |
Neto,A. B. |
author_facet |
Neto,A. B. Hirata,D. B. Cassiano Filho,L. C. M. Bellão,C. Badino Júnior,A. C. Hokka,C. O. |
author_role |
author |
author2 |
Hirata,D. B. Cassiano Filho,L. C. M. Bellão,C. Badino Júnior,A. C. Hokka,C. O. |
author2_role |
author author author author author |
dc.contributor.author.fl_str_mv |
Neto,A. B. Hirata,D. B. Cassiano Filho,L. C. M. Bellão,C. Badino Júnior,A. C. Hokka,C. O. |
dc.subject.por.fl_str_mv |
Clavulanic acid Bioreactors Enzymes |
topic |
Clavulanic acid Bioreactors Enzymes |
description |
Clavulanic acid (CA) is a potent inhibitor of beta-lactamases, enzymes that are responsible for the hydrolysis of beta-lactam antibiotics. It is a secondary metabolite produced by the filamentous aerobic bacterium Streptomyces clavuligerus in submerged cultivations. In the present work clavulanic acid production in batch, fed-batch and continuous bioreactors was studied with the objective of increasing productivity. The operating conditions: temperature, aeration and agitation, were the same in all cases, 28º C, 0.5 vvm and 800 rpm, respectively. The CA concentration obtained in the fed-batch culture, 404 mg L-1, was ca twice the value obtained in the batch culture, 194 mg L-1, while 293 mg L-1 was obtained in the continuous culture. The highest productivity was obtained in the continuous cultivation, 10.6 mg L-1 h-1, as compared with 8.8 mg L-1 h-1 in the fed-batch process and 3.5 mg L-1 h-1 in the batch process, suggesting that continuous culture of Streptomyces clavuligerus is a promising strategy for clavulanic acid production. |
publishDate |
2005 |
dc.date.none.fl_str_mv |
2005-12-01 |
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=S0104-66322005000400008 |
url |
http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322005000400008 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
10.1590/S0104-66322005000400008 |
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.22 n.4 2005 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_ |
1754213171928760320 |