Continuous Long-Term Anaerobic Co-digestion of Crude Glycerol and Domestic Sewage: Plug-Flow In-Series Reactor Performance and Microbiota Acclimatization
Autor(a) principal: | |
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Data de Publicação: | 2022 |
Outros Autores: | , |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | Repositório Institucional da UNESP |
Texto Completo: | http://dx.doi.org/10.1007/s12155-022-10515-0 http://hdl.handle.net/11449/237972 |
Resumo: | Long-term operation of four in-series horizontal anaerobic reactors with fixed bed (HARFB) R1, R2, R3, and R4 was conducted to evaluate the co-digestion of domestic sewage (DS) with different proportions of crude glycerol (CG) from biodiesel production. The main objective was to examine the effect of the increase of CG in the influent with the proportions of 1.5%, 2%, and 3% (v/v). The anaerobic co-digestion was conducted in sequential reactors with increasing diameters to favor the fermentation in the R1 and R2 and the methanogenesis in the R3 and R4. The increase in CG proportions in the influent resulted in mean OLRs of 18.06, 26.75, and 37.85 kg COD/(m(3) day) for 1.5%, 2%, and 3% of CG, respectively. The highest hydrogen production was (L H-2/(m(3) day)) 277.88 (R1, at the 1.5% CG) and 84.43 (R2, at the 2% CG). The highest methane volumetric production occurred during the 1.5% CG in R3 (306.7 L CH4/(m(3) day)), with a 98% COD removal. The configuration of four in-series reactors could promote total removals of CG, even at the 3% CG. Reactor R1 produced 4 g/L of 1,3-propanediol and 2.8 g/L of propionic acid. The changes in the microbiota were verified, mainly on how the Lactobacillales and Selenomonadales orders were favored, respectively, in the fermentative reactor (R1) and the methanogenic reactor (R3). The inhibition of the methanogens verified in the in-series reactors selected the Methanosarcinales order. Even though CG increased caused some instabilities in the reactor parameters, no toxic effect was reached and the HARFB in-series system showed robustness to removing CG continuously for extended times. |
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Continuous Long-Term Anaerobic Co-digestion of Crude Glycerol and Domestic Sewage: Plug-Flow In-Series Reactor Performance and Microbiota AcclimatizationBiogasHydrogenMethaneBiodieselAnaerobic reactor1,3-PropanediolLong-term operation of four in-series horizontal anaerobic reactors with fixed bed (HARFB) R1, R2, R3, and R4 was conducted to evaluate the co-digestion of domestic sewage (DS) with different proportions of crude glycerol (CG) from biodiesel production. The main objective was to examine the effect of the increase of CG in the influent with the proportions of 1.5%, 2%, and 3% (v/v). The anaerobic co-digestion was conducted in sequential reactors with increasing diameters to favor the fermentation in the R1 and R2 and the methanogenesis in the R3 and R4. The increase in CG proportions in the influent resulted in mean OLRs of 18.06, 26.75, and 37.85 kg COD/(m(3) day) for 1.5%, 2%, and 3% of CG, respectively. The highest hydrogen production was (L H-2/(m(3) day)) 277.88 (R1, at the 1.5% CG) and 84.43 (R2, at the 2% CG). The highest methane volumetric production occurred during the 1.5% CG in R3 (306.7 L CH4/(m(3) day)), with a 98% COD removal. The configuration of four in-series reactors could promote total removals of CG, even at the 3% CG. Reactor R1 produced 4 g/L of 1,3-propanediol and 2.8 g/L of propionic acid. The changes in the microbiota were verified, mainly on how the Lactobacillales and Selenomonadales orders were favored, respectively, in the fermentative reactor (R1) and the methanogenic reactor (R3). The inhibition of the methanogens verified in the in-series reactors selected the Methanosarcinales order. Even though CG increased caused some instabilities in the reactor parameters, no toxic effect was reached and the HARFB in-series system showed robustness to removing CG continuously for extended times.Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)Sao Paulo State Univ, Postgrad Program Biotechnol, Inst Chem, UNESP, BR-14800060 Araraquara, SP, BrazilSao Paulo State Univ, IPBEN Bioenergy Res Inst, UNESP, BR-13500230 Rio Claro, SP, BrazilUniv Araraquara, UNIARA, BR-14801320 Araraquara, SP, BrazilSao Paulo State Univ, Postgrad Program Biotechnol, Inst Chem, UNESP, BR-14800060 Araraquara, SP, BrazilSao Paulo State Univ, IPBEN Bioenergy Res Inst, UNESP, BR-13500230 Rio Claro, SP, BrazilCNPq: 407298/2018-5CNPq: 457144/2014-9FAPESP: 2017/11767-1FAPESP: 2017/25329-6CAPES: 001SpringerUniversidade Estadual Paulista (UNESP)Univ AraraquaraAdames, Luan Vieira [UNESP]Pires, Lorena Oliveira [UNESP]Maintinguer, Sandra Imaculada [UNESP]2022-11-30T16:21:04Z2022-11-30T16:21:04Z2022-09-17info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/article13http://dx.doi.org/10.1007/s12155-022-10515-0Bioenergy Research. New York: Springer, 13 p., 2022.1939-1234http://hdl.handle.net/11449/23797210.1007/s12155-022-10515-0WOS:000854855500001Web of Sciencereponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPengBioenergy Researchinfo:eu-repo/semantics/openAccess2022-11-30T16:21:04Zoai:repositorio.unesp.br:11449/237972Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462024-08-05T13:36:55.560506Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)false |
dc.title.none.fl_str_mv |
Continuous Long-Term Anaerobic Co-digestion of Crude Glycerol and Domestic Sewage: Plug-Flow In-Series Reactor Performance and Microbiota Acclimatization |
title |
Continuous Long-Term Anaerobic Co-digestion of Crude Glycerol and Domestic Sewage: Plug-Flow In-Series Reactor Performance and Microbiota Acclimatization |
spellingShingle |
Continuous Long-Term Anaerobic Co-digestion of Crude Glycerol and Domestic Sewage: Plug-Flow In-Series Reactor Performance and Microbiota Acclimatization Adames, Luan Vieira [UNESP] Biogas Hydrogen Methane Biodiesel Anaerobic reactor 1,3-Propanediol |
title_short |
Continuous Long-Term Anaerobic Co-digestion of Crude Glycerol and Domestic Sewage: Plug-Flow In-Series Reactor Performance and Microbiota Acclimatization |
title_full |
Continuous Long-Term Anaerobic Co-digestion of Crude Glycerol and Domestic Sewage: Plug-Flow In-Series Reactor Performance and Microbiota Acclimatization |
title_fullStr |
Continuous Long-Term Anaerobic Co-digestion of Crude Glycerol and Domestic Sewage: Plug-Flow In-Series Reactor Performance and Microbiota Acclimatization |
title_full_unstemmed |
Continuous Long-Term Anaerobic Co-digestion of Crude Glycerol and Domestic Sewage: Plug-Flow In-Series Reactor Performance and Microbiota Acclimatization |
title_sort |
Continuous Long-Term Anaerobic Co-digestion of Crude Glycerol and Domestic Sewage: Plug-Flow In-Series Reactor Performance and Microbiota Acclimatization |
author |
Adames, Luan Vieira [UNESP] |
author_facet |
Adames, Luan Vieira [UNESP] Pires, Lorena Oliveira [UNESP] Maintinguer, Sandra Imaculada [UNESP] |
author_role |
author |
author2 |
Pires, Lorena Oliveira [UNESP] Maintinguer, Sandra Imaculada [UNESP] |
author2_role |
author author |
dc.contributor.none.fl_str_mv |
Universidade Estadual Paulista (UNESP) Univ Araraquara |
dc.contributor.author.fl_str_mv |
Adames, Luan Vieira [UNESP] Pires, Lorena Oliveira [UNESP] Maintinguer, Sandra Imaculada [UNESP] |
dc.subject.por.fl_str_mv |
Biogas Hydrogen Methane Biodiesel Anaerobic reactor 1,3-Propanediol |
topic |
Biogas Hydrogen Methane Biodiesel Anaerobic reactor 1,3-Propanediol |
description |
Long-term operation of four in-series horizontal anaerobic reactors with fixed bed (HARFB) R1, R2, R3, and R4 was conducted to evaluate the co-digestion of domestic sewage (DS) with different proportions of crude glycerol (CG) from biodiesel production. The main objective was to examine the effect of the increase of CG in the influent with the proportions of 1.5%, 2%, and 3% (v/v). The anaerobic co-digestion was conducted in sequential reactors with increasing diameters to favor the fermentation in the R1 and R2 and the methanogenesis in the R3 and R4. The increase in CG proportions in the influent resulted in mean OLRs of 18.06, 26.75, and 37.85 kg COD/(m(3) day) for 1.5%, 2%, and 3% of CG, respectively. The highest hydrogen production was (L H-2/(m(3) day)) 277.88 (R1, at the 1.5% CG) and 84.43 (R2, at the 2% CG). The highest methane volumetric production occurred during the 1.5% CG in R3 (306.7 L CH4/(m(3) day)), with a 98% COD removal. The configuration of four in-series reactors could promote total removals of CG, even at the 3% CG. Reactor R1 produced 4 g/L of 1,3-propanediol and 2.8 g/L of propionic acid. The changes in the microbiota were verified, mainly on how the Lactobacillales and Selenomonadales orders were favored, respectively, in the fermentative reactor (R1) and the methanogenic reactor (R3). The inhibition of the methanogens verified in the in-series reactors selected the Methanosarcinales order. Even though CG increased caused some instabilities in the reactor parameters, no toxic effect was reached and the HARFB in-series system showed robustness to removing CG continuously for extended times. |
publishDate |
2022 |
dc.date.none.fl_str_mv |
2022-11-30T16:21:04Z 2022-11-30T16:21:04Z 2022-09-17 |
dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/article |
format |
article |
status_str |
publishedVersion |
dc.identifier.uri.fl_str_mv |
http://dx.doi.org/10.1007/s12155-022-10515-0 Bioenergy Research. New York: Springer, 13 p., 2022. 1939-1234 http://hdl.handle.net/11449/237972 10.1007/s12155-022-10515-0 WOS:000854855500001 |
url |
http://dx.doi.org/10.1007/s12155-022-10515-0 http://hdl.handle.net/11449/237972 |
identifier_str_mv |
Bioenergy Research. New York: Springer, 13 p., 2022. 1939-1234 10.1007/s12155-022-10515-0 WOS:000854855500001 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
Bioenergy Research |
dc.rights.driver.fl_str_mv |
info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
13 |
dc.publisher.none.fl_str_mv |
Springer |
publisher.none.fl_str_mv |
Springer |
dc.source.none.fl_str_mv |
Web of Science reponame:Repositório Institucional da UNESP instname:Universidade Estadual Paulista (UNESP) instacron:UNESP |
instname_str |
Universidade Estadual Paulista (UNESP) |
instacron_str |
UNESP |
institution |
UNESP |
reponame_str |
Repositório Institucional da UNESP |
collection |
Repositório Institucional da UNESP |
repository.name.fl_str_mv |
Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP) |
repository.mail.fl_str_mv |
|
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1808128254421237760 |