STUDY OF THE REMOVAL OF FERMENTATION INHIBITORS AFTER ACID AND ENZYMATIC TREATMENT OF CANE STRAW
Autor(a) principal: | |
---|---|
Data de Publicação: | 2017 |
Outros Autores: | , , , , , |
Tipo de documento: | Artigo |
Idioma: | por |
Título da fonte: | Revista de Engenharia Química e Química |
Texto Completo: | https://periodicos.ufv.br/jcec/article/view/2446941603022017095 |
Resumo: | It was studied the removal of toxic inhibitors produced during dilute-acid pretreatment of lignocellulosic biomass. Different sulfuric acid concentrations (1%, 2.5% and 5%) and reaction times (15, 30 and 60 minutes) were analyzed for the pretreatment process, and, 1% w/w H2SO4 and 15-minute reaction time have proven to be the most proper condition. With the experimental data, purification and concentration operations were simulated. For C5 stream (xylose, furfural and water) three different unit operations have been explored: a flash drum, a distillation column and a distillation column followed by multiple-effect evaporators. The distillation column with five multiple-effect evaporator system achieved the best energy efficiency (0,85 kW/kg xylose) and removal of furfural. For C6 stream (glucose and water), a four multiple-effect evaporator system simulated showed that the energy requirements not change significantly within the range of sugar concentration used (14% to 20%). |
id |
UFV-4_337f4415ee44f8bf8ae97b76aaa26610 |
---|---|
oai_identifier_str |
oai:ojs.periodicos.ufv.br:article/2306 |
network_acronym_str |
UFV-4 |
network_name_str |
Revista de Engenharia Química e Química |
repository_id_str |
|
spelling |
STUDY OF THE REMOVAL OF FERMENTATION INHIBITORS AFTER ACID AND ENZYMATIC TREATMENT OF CANE STRAWESTUDO DA REMOÇÃO DE INIBIDORES DE FERMENTAÇÃO APÓS TRATAMENTO ÁCIDO E ENZIMÁTICO DE PALHA DE CANAEthanolFurfuralLignocellulosicsAcid pretreatmentBiomassEtanol. FurfuralLignocelulósicosPré-tratamento ácidoBiomassaIt was studied the removal of toxic inhibitors produced during dilute-acid pretreatment of lignocellulosic biomass. Different sulfuric acid concentrations (1%, 2.5% and 5%) and reaction times (15, 30 and 60 minutes) were analyzed for the pretreatment process, and, 1% w/w H2SO4 and 15-minute reaction time have proven to be the most proper condition. With the experimental data, purification and concentration operations were simulated. For C5 stream (xylose, furfural and water) three different unit operations have been explored: a flash drum, a distillation column and a distillation column followed by multiple-effect evaporators. The distillation column with five multiple-effect evaporator system achieved the best energy efficiency (0,85 kW/kg xylose) and removal of furfural. For C6 stream (glucose and water), a four multiple-effect evaporator system simulated showed that the energy requirements not change significantly within the range of sugar concentration used (14% to 20%).Neste trabalho estudou-se a remoção do furfural, inibidor tóxico à fermentação, formado no pré-tratamento ácido de lignocelulósicos. Experimentalmente estudaram-se no pré-tratamento diferentes concentrações de H2SO4 (1%, 2,5% e 5%) e tempos de reação (15, 30 e 60 minutos). Definiu-se como condição mais adequada 1 % m/m de ácido sulfúrico e 15 minutos como tempo de reação. Com os dados experimentais realizou-se a simulação da remoção do furfural e da concentração dos açúcares. As correntes contendo açúcares foram denominadas de C5 (hidrolisado ácido – xilose e furfural) e C6 (hidrolisado enzimático - glicose). A corrente C5 foi purificada e concentrada através de uma coluna de enchimento integrada a evaporadores múltiplos com cinco efeitos, com gasto energético de 0,85 kW/kg de xilose. Para concentrar a corrente C6 de 14 a 20% de açúcares utilizaram-se evaporadores múltiplos com quatro efeitos com gasto energético requerido de 0,34 kW/ kg de glicose.Universidade Federal de Viçosa - UFV2017-03-19info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionapplication/pdfhttps://periodicos.ufv.br/jcec/article/view/244694160302201709510.18540/jcecvl3iss2pp095-111The Journal of Engineering and Exact Sciences; Vol. 3 No. 2 (2017); 095-111The Journal of Engineering and Exact Sciences; Vol. 3 Núm. 2 (2017); 095-111The Journal of Engineering and Exact Sciences; v. 3 n. 2 (2017); 095-1112527-1075reponame:Revista de Engenharia Química e Químicainstname:Universidade Federal de Viçosa (UFV)instacron:UFVporhttps://periodicos.ufv.br/jcec/article/view/2446941603022017095/pdfLucarini, Adriana CéliaFerreira, Newton Libâniode Souza, Charles DouglasFrancisco, Felippe Pinheiro LimaFonseca, Isabela ReinaudRossi, Larissa GuedesFerreira, Vanuza Magalhãesinfo:eu-repo/semantics/openAccess2020-07-14T22:30:57Zoai:ojs.periodicos.ufv.br:article/2306Revistahttp://www.seer.ufv.br/seer/rbeq2/index.php/req2/indexONGhttps://periodicos.ufv.br/jcec/oaijcec.journal@ufv.br||req2@ufv.br2446-94162446-9416opendoar:2020-07-14T22:30:57Revista de Engenharia Química e Química - Universidade Federal de Viçosa (UFV)false |
dc.title.none.fl_str_mv |
STUDY OF THE REMOVAL OF FERMENTATION INHIBITORS AFTER ACID AND ENZYMATIC TREATMENT OF CANE STRAW ESTUDO DA REMOÇÃO DE INIBIDORES DE FERMENTAÇÃO APÓS TRATAMENTO ÁCIDO E ENZIMÁTICO DE PALHA DE CANA |
title |
STUDY OF THE REMOVAL OF FERMENTATION INHIBITORS AFTER ACID AND ENZYMATIC TREATMENT OF CANE STRAW |
spellingShingle |
STUDY OF THE REMOVAL OF FERMENTATION INHIBITORS AFTER ACID AND ENZYMATIC TREATMENT OF CANE STRAW Lucarini, Adriana Célia Ethanol Furfural Lignocellulosics Acid pretreatment Biomass Etanol. Furfural Lignocelulósicos Pré-tratamento ácido Biomassa |
title_short |
STUDY OF THE REMOVAL OF FERMENTATION INHIBITORS AFTER ACID AND ENZYMATIC TREATMENT OF CANE STRAW |
title_full |
STUDY OF THE REMOVAL OF FERMENTATION INHIBITORS AFTER ACID AND ENZYMATIC TREATMENT OF CANE STRAW |
title_fullStr |
STUDY OF THE REMOVAL OF FERMENTATION INHIBITORS AFTER ACID AND ENZYMATIC TREATMENT OF CANE STRAW |
title_full_unstemmed |
STUDY OF THE REMOVAL OF FERMENTATION INHIBITORS AFTER ACID AND ENZYMATIC TREATMENT OF CANE STRAW |
title_sort |
STUDY OF THE REMOVAL OF FERMENTATION INHIBITORS AFTER ACID AND ENZYMATIC TREATMENT OF CANE STRAW |
author |
Lucarini, Adriana Célia |
author_facet |
Lucarini, Adriana Célia Ferreira, Newton Libânio de Souza, Charles Douglas Francisco, Felippe Pinheiro Lima Fonseca, Isabela Reinaud Rossi, Larissa Guedes Ferreira, Vanuza Magalhães |
author_role |
author |
author2 |
Ferreira, Newton Libânio de Souza, Charles Douglas Francisco, Felippe Pinheiro Lima Fonseca, Isabela Reinaud Rossi, Larissa Guedes Ferreira, Vanuza Magalhães |
author2_role |
author author author author author author |
dc.contributor.author.fl_str_mv |
Lucarini, Adriana Célia Ferreira, Newton Libânio de Souza, Charles Douglas Francisco, Felippe Pinheiro Lima Fonseca, Isabela Reinaud Rossi, Larissa Guedes Ferreira, Vanuza Magalhães |
dc.subject.por.fl_str_mv |
Ethanol Furfural Lignocellulosics Acid pretreatment Biomass Etanol. Furfural Lignocelulósicos Pré-tratamento ácido Biomassa |
topic |
Ethanol Furfural Lignocellulosics Acid pretreatment Biomass Etanol. Furfural Lignocelulósicos Pré-tratamento ácido Biomassa |
description |
It was studied the removal of toxic inhibitors produced during dilute-acid pretreatment of lignocellulosic biomass. Different sulfuric acid concentrations (1%, 2.5% and 5%) and reaction times (15, 30 and 60 minutes) were analyzed for the pretreatment process, and, 1% w/w H2SO4 and 15-minute reaction time have proven to be the most proper condition. With the experimental data, purification and concentration operations were simulated. For C5 stream (xylose, furfural and water) three different unit operations have been explored: a flash drum, a distillation column and a distillation column followed by multiple-effect evaporators. The distillation column with five multiple-effect evaporator system achieved the best energy efficiency (0,85 kW/kg xylose) and removal of furfural. For C6 stream (glucose and water), a four multiple-effect evaporator system simulated showed that the energy requirements not change significantly within the range of sugar concentration used (14% to 20%). |
publishDate |
2017 |
dc.date.none.fl_str_mv |
2017-03-19 |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/article info:eu-repo/semantics/publishedVersion |
format |
article |
status_str |
publishedVersion |
dc.identifier.uri.fl_str_mv |
https://periodicos.ufv.br/jcec/article/view/2446941603022017095 10.18540/jcecvl3iss2pp095-111 |
url |
https://periodicos.ufv.br/jcec/article/view/2446941603022017095 |
identifier_str_mv |
10.18540/jcecvl3iss2pp095-111 |
dc.language.iso.fl_str_mv |
por |
language |
por |
dc.relation.none.fl_str_mv |
https://periodicos.ufv.br/jcec/article/view/2446941603022017095/pdf |
dc.rights.driver.fl_str_mv |
info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
application/pdf |
dc.publisher.none.fl_str_mv |
Universidade Federal de Viçosa - UFV |
publisher.none.fl_str_mv |
Universidade Federal de Viçosa - UFV |
dc.source.none.fl_str_mv |
The Journal of Engineering and Exact Sciences; Vol. 3 No. 2 (2017); 095-111 The Journal of Engineering and Exact Sciences; Vol. 3 Núm. 2 (2017); 095-111 The Journal of Engineering and Exact Sciences; v. 3 n. 2 (2017); 095-111 2527-1075 reponame:Revista de Engenharia Química e Química instname:Universidade Federal de Viçosa (UFV) instacron:UFV |
instname_str |
Universidade Federal de Viçosa (UFV) |
instacron_str |
UFV |
institution |
UFV |
reponame_str |
Revista de Engenharia Química e Química |
collection |
Revista de Engenharia Química e Química |
repository.name.fl_str_mv |
Revista de Engenharia Química e Química - Universidade Federal de Viçosa (UFV) |
repository.mail.fl_str_mv |
jcec.journal@ufv.br||req2@ufv.br |
_version_ |
1800211187505299456 |