Laying hen manure in anaerobic Co-Digestion with glycerin containing different glycerol and impurity levels
Autor(a) principal: | |
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Data de Publicação: | 2019 |
Outros Autores: | , , , , |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | Repositório Institucional da UNESP |
Texto Completo: | http://dx.doi.org/10.1016/j.jclepro.2019.01.125 http://hdl.handle.net/11449/186649 |
Resumo: | Biodiesel has arisen as a promising option of renewable fuel to minimize the impacts caused by fossil fuels. However, its production process generates high amounts of crude glycerin as a residue, which is considered low-quality commercially due to its low glycerol content. In order to add value to this byproduct, some production plants employ a purification process. Nonetheless, aiming to cut down costs with this purification step, many researches have been seeking treatments that use glycerin with lower purity, such as anaerobic co-digestion with another residue of complementary composition so as to balance the digestion medium and increase energy yield. During recycling, glycerin goes from an environmental liability to a sustainable financial asset by being transformed into cleaner energy, i.e., biogas. This research was carried out to assess the influence of glycerol content in glycerin containing the same impurities at three proportions (40% (G40), 60% (G60), and 80% (G80)), and to add them to the process at different glycerol levels (0, 1, 2, 3, and 4%) in the total solids (TS) of the affluents prepared with laying hen manure. No interaction was found between glycerin type and glycerol content regarding biogas and methane productions as well as reductions in TS and volatile solids (VS). Adding 2.5% glycerol led to the highest specific biogas production (1654.1 L kg(-1) VS added) while adding 2.6% yielded the maximum specific production of methane (1058.9 L kg(-1) VS added), i.e., glycerol increased methane generation by over 36% when compared with the treatment with no glycerin. Consequently, greater reductions in TS (60.97%) and VS (73.6%) were observed with ideal addition levels of 2.2 and 2.4% glycerol. Adding 2.1% glycerol using G40 resulted in the greatest reduction (55.4%) in chemical oxygen demand (COD) whereas such reduction was by 50.4 and 50.5% for G60 and G80 when 2.6% glycerol were added. With that in mind, and in face of the high costs of purification, G40 can be recommended with addition of 2.6% glycerol to TS to improve co-digestion with laying hen manure and generate energy that returns to poultry and biodiesel production systems. (C) 2019 Elsevier Ltd. All rights reserved. |
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Laying hen manure in anaerobic Co-Digestion with glycerin containing different glycerol and impurity levelsBatch digestionBiodiesel wasteGlycerin purity levelMethane productionBiodiesel has arisen as a promising option of renewable fuel to minimize the impacts caused by fossil fuels. However, its production process generates high amounts of crude glycerin as a residue, which is considered low-quality commercially due to its low glycerol content. In order to add value to this byproduct, some production plants employ a purification process. Nonetheless, aiming to cut down costs with this purification step, many researches have been seeking treatments that use glycerin with lower purity, such as anaerobic co-digestion with another residue of complementary composition so as to balance the digestion medium and increase energy yield. During recycling, glycerin goes from an environmental liability to a sustainable financial asset by being transformed into cleaner energy, i.e., biogas. This research was carried out to assess the influence of glycerol content in glycerin containing the same impurities at three proportions (40% (G40), 60% (G60), and 80% (G80)), and to add them to the process at different glycerol levels (0, 1, 2, 3, and 4%) in the total solids (TS) of the affluents prepared with laying hen manure. No interaction was found between glycerin type and glycerol content regarding biogas and methane productions as well as reductions in TS and volatile solids (VS). Adding 2.5% glycerol led to the highest specific biogas production (1654.1 L kg(-1) VS added) while adding 2.6% yielded the maximum specific production of methane (1058.9 L kg(-1) VS added), i.e., glycerol increased methane generation by over 36% when compared with the treatment with no glycerin. Consequently, greater reductions in TS (60.97%) and VS (73.6%) were observed with ideal addition levels of 2.2 and 2.4% glycerol. Adding 2.1% glycerol using G40 resulted in the greatest reduction (55.4%) in chemical oxygen demand (COD) whereas such reduction was by 50.4 and 50.5% for G60 and G80 when 2.6% glycerol were added. With that in mind, and in face of the high costs of purification, G40 can be recommended with addition of 2.6% glycerol to TS to improve co-digestion with laying hen manure and generate energy that returns to poultry and biodiesel production systems. (C) 2019 Elsevier Ltd. All rights reserved.Sao Paulo State University Julio de Mesquita Filho (UNESP)Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)Fed Univ Great Dourados, Sch Agr Sci, POB 364, BR-79804970 Dourados, MS, BrazilState Univ Sao Paulo Julio de Mesquita Filho, Sch Vet Med & Anim Sci, BR-14884900 Jaboticabal, SP, BrazilWest Parana State Univ, Ctr Engn & Exact Sci, BR-85819110 Toledo, PR, BrazilState Univ Sao Paulo Julio de Mesquita Filho, Sch Vet Med & Anim Sci, BR-14884900 Jaboticabal, SP, BrazilElsevier B.V.Fed Univ Great DouradosUniversidade Estadual Paulista (Unesp)West Parana State UnivSchwingel, Alice WatteAmorim Orrico, Ana CarolinaLucas Junior, Jorge de [UNESP]Previdelli Orrico Junior, Marco AntonioAspilcueta Borquis, Rusbel RaulFava, Aldo Felipe2019-10-05T14:08:27Z2019-10-05T14:08:27Z2019-04-01info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/article1437-1444http://dx.doi.org/10.1016/j.jclepro.2019.01.125Journal Of Cleaner Production. Oxford: Elsevier Sci Ltd, v. 215, p. 1437-1444, 2019.0959-6526http://hdl.handle.net/11449/18664910.1016/j.jclepro.2019.01.125WOS:000459358300120Web of Sciencereponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPengJournal Of Cleaner Productioninfo:eu-repo/semantics/openAccess2024-06-06T15:18:29Zoai:repositorio.unesp.br:11449/186649Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462024-08-05T18:01:50.731615Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)false |
dc.title.none.fl_str_mv |
Laying hen manure in anaerobic Co-Digestion with glycerin containing different glycerol and impurity levels |
title |
Laying hen manure in anaerobic Co-Digestion with glycerin containing different glycerol and impurity levels |
spellingShingle |
Laying hen manure in anaerobic Co-Digestion with glycerin containing different glycerol and impurity levels Schwingel, Alice Watte Batch digestion Biodiesel waste Glycerin purity level Methane production |
title_short |
Laying hen manure in anaerobic Co-Digestion with glycerin containing different glycerol and impurity levels |
title_full |
Laying hen manure in anaerobic Co-Digestion with glycerin containing different glycerol and impurity levels |
title_fullStr |
Laying hen manure in anaerobic Co-Digestion with glycerin containing different glycerol and impurity levels |
title_full_unstemmed |
Laying hen manure in anaerobic Co-Digestion with glycerin containing different glycerol and impurity levels |
title_sort |
Laying hen manure in anaerobic Co-Digestion with glycerin containing different glycerol and impurity levels |
author |
Schwingel, Alice Watte |
author_facet |
Schwingel, Alice Watte Amorim Orrico, Ana Carolina Lucas Junior, Jorge de [UNESP] Previdelli Orrico Junior, Marco Antonio Aspilcueta Borquis, Rusbel Raul Fava, Aldo Felipe |
author_role |
author |
author2 |
Amorim Orrico, Ana Carolina Lucas Junior, Jorge de [UNESP] Previdelli Orrico Junior, Marco Antonio Aspilcueta Borquis, Rusbel Raul Fava, Aldo Felipe |
author2_role |
author author author author author |
dc.contributor.none.fl_str_mv |
Fed Univ Great Dourados Universidade Estadual Paulista (Unesp) West Parana State Univ |
dc.contributor.author.fl_str_mv |
Schwingel, Alice Watte Amorim Orrico, Ana Carolina Lucas Junior, Jorge de [UNESP] Previdelli Orrico Junior, Marco Antonio Aspilcueta Borquis, Rusbel Raul Fava, Aldo Felipe |
dc.subject.por.fl_str_mv |
Batch digestion Biodiesel waste Glycerin purity level Methane production |
topic |
Batch digestion Biodiesel waste Glycerin purity level Methane production |
description |
Biodiesel has arisen as a promising option of renewable fuel to minimize the impacts caused by fossil fuels. However, its production process generates high amounts of crude glycerin as a residue, which is considered low-quality commercially due to its low glycerol content. In order to add value to this byproduct, some production plants employ a purification process. Nonetheless, aiming to cut down costs with this purification step, many researches have been seeking treatments that use glycerin with lower purity, such as anaerobic co-digestion with another residue of complementary composition so as to balance the digestion medium and increase energy yield. During recycling, glycerin goes from an environmental liability to a sustainable financial asset by being transformed into cleaner energy, i.e., biogas. This research was carried out to assess the influence of glycerol content in glycerin containing the same impurities at three proportions (40% (G40), 60% (G60), and 80% (G80)), and to add them to the process at different glycerol levels (0, 1, 2, 3, and 4%) in the total solids (TS) of the affluents prepared with laying hen manure. No interaction was found between glycerin type and glycerol content regarding biogas and methane productions as well as reductions in TS and volatile solids (VS). Adding 2.5% glycerol led to the highest specific biogas production (1654.1 L kg(-1) VS added) while adding 2.6% yielded the maximum specific production of methane (1058.9 L kg(-1) VS added), i.e., glycerol increased methane generation by over 36% when compared with the treatment with no glycerin. Consequently, greater reductions in TS (60.97%) and VS (73.6%) were observed with ideal addition levels of 2.2 and 2.4% glycerol. Adding 2.1% glycerol using G40 resulted in the greatest reduction (55.4%) in chemical oxygen demand (COD) whereas such reduction was by 50.4 and 50.5% for G60 and G80 when 2.6% glycerol were added. With that in mind, and in face of the high costs of purification, G40 can be recommended with addition of 2.6% glycerol to TS to improve co-digestion with laying hen manure and generate energy that returns to poultry and biodiesel production systems. (C) 2019 Elsevier Ltd. All rights reserved. |
publishDate |
2019 |
dc.date.none.fl_str_mv |
2019-10-05T14:08:27Z 2019-10-05T14:08:27Z 2019-04-01 |
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/10.1016/j.jclepro.2019.01.125 Journal Of Cleaner Production. Oxford: Elsevier Sci Ltd, v. 215, p. 1437-1444, 2019. 0959-6526 http://hdl.handle.net/11449/186649 10.1016/j.jclepro.2019.01.125 WOS:000459358300120 |
url |
http://dx.doi.org/10.1016/j.jclepro.2019.01.125 http://hdl.handle.net/11449/186649 |
identifier_str_mv |
Journal Of Cleaner Production. Oxford: Elsevier Sci Ltd, v. 215, p. 1437-1444, 2019. 0959-6526 10.1016/j.jclepro.2019.01.125 WOS:000459358300120 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
Journal Of Cleaner Production |
dc.rights.driver.fl_str_mv |
info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
1437-1444 |
dc.publisher.none.fl_str_mv |
Elsevier B.V. |
publisher.none.fl_str_mv |
Elsevier B.V. |
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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1808128886907600896 |