Expanded bed adsorption of bromelain (E.C. 3.4.22.33) from Ananas comosus crude extract
Autor(a) principal: | |
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Data de Publicação: | 2009 |
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=S0104-66322009000100014 |
Resumo: | This work focuses on the adsorption of Bromelain in expanded bed conditions, such as the adsorption kinetics parameters. The adsorption kinetics parameters showed that after 40 minutes equilibrium was achieved and maximum adsorption capacity was 6.11 U per resin mL. However, the maximum adsorption capacity was only determined by measuring the adsorption isotherm. Only by the Langmuir model the maximum adsorption capacity, Qm, and dissociation constant, kd, values could be estimated as 9.18 U/mL and 0.591, respectively, at 25 ºC and 0.1 mol/L phosphate buffer pH 7.5. A column made of glass with an inner diameter of 1 cm was used for the expanded bed adsorption (EBA). The residence time was reduced 10 fold by increasing the expansion degree 2.5 times; nonetheless, the plate number (N) value was reduced only 2 fold. After adsorption, the bromelain was eluted in packed bed mode, with a downward flow. The purification factor was about 13 fold and the total protein was reduced 4 fold. EBA showed to be feasible for purification of bromelain. |
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Expanded bed adsorption of bromelain (E.C. 3.4.22.33) from Ananas comosus crude extractAdsorptionEnzyme ActivityPurificationAxial DispersionExpanded Bed AdsorptionBromelainThis work focuses on the adsorption of Bromelain in expanded bed conditions, such as the adsorption kinetics parameters. The adsorption kinetics parameters showed that after 40 minutes equilibrium was achieved and maximum adsorption capacity was 6.11 U per resin mL. However, the maximum adsorption capacity was only determined by measuring the adsorption isotherm. Only by the Langmuir model the maximum adsorption capacity, Qm, and dissociation constant, kd, values could be estimated as 9.18 U/mL and 0.591, respectively, at 25 ºC and 0.1 mol/L phosphate buffer pH 7.5. A column made of glass with an inner diameter of 1 cm was used for the expanded bed adsorption (EBA). The residence time was reduced 10 fold by increasing the expansion degree 2.5 times; nonetheless, the plate number (N) value was reduced only 2 fold. After adsorption, the bromelain was eluted in packed bed mode, with a downward flow. The purification factor was about 13 fold and the total protein was reduced 4 fold. EBA showed to be feasible for purification of bromelain.Brazilian Society of Chemical Engineering2009-03-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322009000100014Brazilian Journal of Chemical Engineering v.26 n.1 2009reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/S0104-66322009000100014info:eu-repo/semantics/openAccessSilveira,E.Souza-Jr,M. E.Santana,J. C. C.Chaves,A. C.Porto,L. F.Tambourgi,E. Beng2009-03-10T00:00:00Zoai:scielo:S0104-66322009000100014Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:2009-03-10T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false |
dc.title.none.fl_str_mv |
Expanded bed adsorption of bromelain (E.C. 3.4.22.33) from Ananas comosus crude extract |
title |
Expanded bed adsorption of bromelain (E.C. 3.4.22.33) from Ananas comosus crude extract |
spellingShingle |
Expanded bed adsorption of bromelain (E.C. 3.4.22.33) from Ananas comosus crude extract Silveira,E. Adsorption Enzyme Activity Purification Axial Dispersion Expanded Bed Adsorption Bromelain |
title_short |
Expanded bed adsorption of bromelain (E.C. 3.4.22.33) from Ananas comosus crude extract |
title_full |
Expanded bed adsorption of bromelain (E.C. 3.4.22.33) from Ananas comosus crude extract |
title_fullStr |
Expanded bed adsorption of bromelain (E.C. 3.4.22.33) from Ananas comosus crude extract |
title_full_unstemmed |
Expanded bed adsorption of bromelain (E.C. 3.4.22.33) from Ananas comosus crude extract |
title_sort |
Expanded bed adsorption of bromelain (E.C. 3.4.22.33) from Ananas comosus crude extract |
author |
Silveira,E. |
author_facet |
Silveira,E. Souza-Jr,M. E. Santana,J. C. C. Chaves,A. C. Porto,L. F. Tambourgi,E. B |
author_role |
author |
author2 |
Souza-Jr,M. E. Santana,J. C. C. Chaves,A. C. Porto,L. F. Tambourgi,E. B |
author2_role |
author author author author author |
dc.contributor.author.fl_str_mv |
Silveira,E. Souza-Jr,M. E. Santana,J. C. C. Chaves,A. C. Porto,L. F. Tambourgi,E. B |
dc.subject.por.fl_str_mv |
Adsorption Enzyme Activity Purification Axial Dispersion Expanded Bed Adsorption Bromelain |
topic |
Adsorption Enzyme Activity Purification Axial Dispersion Expanded Bed Adsorption Bromelain |
description |
This work focuses on the adsorption of Bromelain in expanded bed conditions, such as the adsorption kinetics parameters. The adsorption kinetics parameters showed that after 40 minutes equilibrium was achieved and maximum adsorption capacity was 6.11 U per resin mL. However, the maximum adsorption capacity was only determined by measuring the adsorption isotherm. Only by the Langmuir model the maximum adsorption capacity, Qm, and dissociation constant, kd, values could be estimated as 9.18 U/mL and 0.591, respectively, at 25 ºC and 0.1 mol/L phosphate buffer pH 7.5. A column made of glass with an inner diameter of 1 cm was used for the expanded bed adsorption (EBA). The residence time was reduced 10 fold by increasing the expansion degree 2.5 times; nonetheless, the plate number (N) value was reduced only 2 fold. After adsorption, the bromelain was eluted in packed bed mode, with a downward flow. The purification factor was about 13 fold and the total protein was reduced 4 fold. EBA showed to be feasible for purification of bromelain. |
publishDate |
2009 |
dc.date.none.fl_str_mv |
2009-03-01 |
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=S0104-66322009000100014 |
url |
http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322009000100014 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
10.1590/S0104-66322009000100014 |
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.26 n.1 2009 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_ |
1754213172735115264 |