Busca avançada
Ano de início
Entree
(Referência obtida automaticamente do Web of Science, por meio da informação sobre o financiamento pela FAPESP e o número do processo correspondente, incluída na publicação pelos autores.)

Sequential fermentative and phototrophic system for hydrogen production: An approach for Brazilian alcohol distillery wastewater

Texto completo
Autor(es):
Lazaro, Carolina Zampol [1] ; Varesche, Maria Bernadete A. [2] ; Silva, Edson Luiz [1]
Número total de Autores: 3
Afiliação do(s) autor(es):
[1] Univ Fed Sao Carlos, Dept Chem Engn, BR-13565905 Sao Carlos, SP - Brazil
[2] Univ Sao Paulo, Sch Engn Sao Carlos, Dept Hydraul & Sanitat, BR-13566590 Sao Carlos, SP - Brazil
Número total de Afiliações: 2
Tipo de documento: Artigo Científico
Fonte: INTERNATIONAL JOURNAL OF HYDROGEN ENERGY; v. 40, n. 31, p. 9642-9655, AUG 17 2015.
Citações Web of Science: 10
Resumo

This study evaluated the possibility of using sugarcane vinasse for biological hydrogen production under non-sterile conditions via sequential two-stage fermentative and phototrophic processes, which simultaneously allows bioenergy production and chemical oxygen demand (COD) removal. The fermentative process was performed in an anaerobic fluidized bed reactor (AFBR) fed with a mixture of sucrose and sugarcane vinasse (5:10 g COD L-1). The phototrophic process was performed using a microbial consortium (Rhodopseudomonas related microorganisms) as inoculum and batch reactors fed with different concentrations of the AFBR effluent (10, 20, 40, 70 and 80%, v/v). The hydrogen yield (HY) (0.34 mol H-2 g(-1) CODinfluent) observed in the fermentative step was justified by the establishment of microbial community composed predominantly by Lactobacillus related microorganisms. The highest HY observed in the phototrophic stage (5.5 mmol H-2 g(-1) CODremoved) was observed for the lowest AFBR concentration. Increasing the AFBR effluent concentration as the substrate for the phototrophic reactors had a negative impact on cell growth, hydrogen production and COD removal mostly due to the occurrence of sulfate reduction. Hydrogen production was not observed in batch reactors fed with 70 and 80% of AFBR effluent; however, under those conditions, the sulfate removal rate was 86.5 and 86.9%, respectively. Copyright (C) 2015, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved. (AU)

Processo FAPESP: 09/15984-0 - Produção de bioenergia no tratamento de águas residuárias e adequação ambiental dos efluentes e resíduos gerados
Beneficiário:Marcelo Zaiat
Modalidade de apoio: Auxílio à Pesquisa - Temático
Processo FAPESP: 12/21715-5 - Produção de hidrogênio em reator anaeróbio de leito fluidificado tratando vinhaça sob condições termofílicas
Beneficiário:Edson Luiz Silva
Modalidade de apoio: Auxílio à Pesquisa - Regular
Processo FAPESP: 12/03979-5 - Sistema seqüencial fermentativo/fotossintético para produção de hidrogênio a partir de vinhaça de cana-de-açúcar
Beneficiário:Carolina Zampol Lazaro
Modalidade de apoio: Bolsas no Brasil - Pós-Doutorado