One-pot fungal biomass-to-biodiesel process: Influence of the molar ratio and the concentration of acid heterogenous catalyst on reaction yield and costs

Detalhes bibliográficos
Autor(a) principal: Bento, Heitor B.S. [UNESP]
Data de Publicação: 2021
Outros Autores: Reis, Cristiano E.R., Cunha, Pietro G., Carvalho, Ana K.F., De Castro, Heizir F.
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Institucional da UNESP
Texto Completo: http://dx.doi.org/10.1016/j.fuel.2021.120968
http://hdl.handle.net/11449/206300
Resumo: This work evaluates a microbial-based biodiesel production process through simultaneous esterification and transesterification of the lipid-rich fungal biomass using ethanol as both extractor and acyl acceptor. Two of the most influential parameters were evaluated, the molar ratio of ethanol to the oil, and the concentration of a heterogeneous acid catalyst (H3PMo/Al2O3), with responses in terms of conversion to ethyl esters and an estimated cost of the process variables. Fungal biomass of Mucor circinelloides was cultivated in sugarcane molasses media and the obtained oleaginous cells were used as the source of acylglycerols and free fatty acids for the trans/esterification reactions in a pressurized stainless-steel reactor at 200 °C for 6 h. Our results demonstrate that the effects of the two factors analyzed were significant, with an indication that increases in the molar ratio and catalyst favor the reaction yield. In the reaction system, a molar ratio of 120:1 (ethanol: oil) and 15 wt% of catalyst yielded 96.6% of ester content, which meets the minimum limit established by the international standards. Production costs were estimated in function of ethanol and catalyst price and indicated the selected parameters reflected the adequate configuration to reach the stablished minimum ester content.
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spelling One-pot fungal biomass-to-biodiesel process: Influence of the molar ratio and the concentration of acid heterogenous catalyst on reaction yield and costsBiodieselDirect transesterificationFilamentous fungiHeterogeneous catalysisSingle cell oilThis work evaluates a microbial-based biodiesel production process through simultaneous esterification and transesterification of the lipid-rich fungal biomass using ethanol as both extractor and acyl acceptor. Two of the most influential parameters were evaluated, the molar ratio of ethanol to the oil, and the concentration of a heterogeneous acid catalyst (H3PMo/Al2O3), with responses in terms of conversion to ethyl esters and an estimated cost of the process variables. Fungal biomass of Mucor circinelloides was cultivated in sugarcane molasses media and the obtained oleaginous cells were used as the source of acylglycerols and free fatty acids for the trans/esterification reactions in a pressurized stainless-steel reactor at 200 °C for 6 h. Our results demonstrate that the effects of the two factors analyzed were significant, with an indication that increases in the molar ratio and catalyst favor the reaction yield. In the reaction system, a molar ratio of 120:1 (ethanol: oil) and 15 wt% of catalyst yielded 96.6% of ester content, which meets the minimum limit established by the international standards. Production costs were estimated in function of ethanol and catalyst price and indicated the selected parameters reflected the adequate configuration to reach the stablished minimum ester content.Engineering School of Lorena University of São Paulo LorenaDepartment of Bioprocess Engineering and Biotechnology School of Pharmaceutical Sciences São Paulo State University - UNESPEARTH UniversityInstitute of Chemistry Federal University of AlfenasDepartment of Bioprocess Engineering and Biotechnology School of Pharmaceutical Sciences São Paulo State University - UNESPUniversidade de São Paulo (USP)Universidade Estadual Paulista (Unesp)EARTH UniversityFederal University of AlfenasBento, Heitor B.S. [UNESP]Reis, Cristiano E.R.Cunha, Pietro G.Carvalho, Ana K.F.De Castro, Heizir F.2021-06-25T10:29:49Z2021-06-25T10:29:49Z2021-09-15info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articlehttp://dx.doi.org/10.1016/j.fuel.2021.120968Fuel, v. 300.0016-2361http://hdl.handle.net/11449/20630010.1016/j.fuel.2021.1209682-s2.0-85105282710Scopusreponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPengFuelinfo:eu-repo/semantics/openAccess2021-10-23T03:04:09Zoai:repositorio.unesp.br:11449/206300Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462021-10-23T03:04:09Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)false
dc.title.none.fl_str_mv One-pot fungal biomass-to-biodiesel process: Influence of the molar ratio and the concentration of acid heterogenous catalyst on reaction yield and costs
title One-pot fungal biomass-to-biodiesel process: Influence of the molar ratio and the concentration of acid heterogenous catalyst on reaction yield and costs
spellingShingle One-pot fungal biomass-to-biodiesel process: Influence of the molar ratio and the concentration of acid heterogenous catalyst on reaction yield and costs
Bento, Heitor B.S. [UNESP]
Biodiesel
Direct transesterification
Filamentous fungi
Heterogeneous catalysis
Single cell oil
title_short One-pot fungal biomass-to-biodiesel process: Influence of the molar ratio and the concentration of acid heterogenous catalyst on reaction yield and costs
title_full One-pot fungal biomass-to-biodiesel process: Influence of the molar ratio and the concentration of acid heterogenous catalyst on reaction yield and costs
title_fullStr One-pot fungal biomass-to-biodiesel process: Influence of the molar ratio and the concentration of acid heterogenous catalyst on reaction yield and costs
title_full_unstemmed One-pot fungal biomass-to-biodiesel process: Influence of the molar ratio and the concentration of acid heterogenous catalyst on reaction yield and costs
title_sort One-pot fungal biomass-to-biodiesel process: Influence of the molar ratio and the concentration of acid heterogenous catalyst on reaction yield and costs
author Bento, Heitor B.S. [UNESP]
author_facet Bento, Heitor B.S. [UNESP]
Reis, Cristiano E.R.
Cunha, Pietro G.
Carvalho, Ana K.F.
De Castro, Heizir F.
author_role author
author2 Reis, Cristiano E.R.
Cunha, Pietro G.
Carvalho, Ana K.F.
De Castro, Heizir F.
author2_role author
author
author
author
dc.contributor.none.fl_str_mv Universidade de São Paulo (USP)
Universidade Estadual Paulista (Unesp)
EARTH University
Federal University of Alfenas
dc.contributor.author.fl_str_mv Bento, Heitor B.S. [UNESP]
Reis, Cristiano E.R.
Cunha, Pietro G.
Carvalho, Ana K.F.
De Castro, Heizir F.
dc.subject.por.fl_str_mv Biodiesel
Direct transesterification
Filamentous fungi
Heterogeneous catalysis
Single cell oil
topic Biodiesel
Direct transesterification
Filamentous fungi
Heterogeneous catalysis
Single cell oil
description This work evaluates a microbial-based biodiesel production process through simultaneous esterification and transesterification of the lipid-rich fungal biomass using ethanol as both extractor and acyl acceptor. Two of the most influential parameters were evaluated, the molar ratio of ethanol to the oil, and the concentration of a heterogeneous acid catalyst (H3PMo/Al2O3), with responses in terms of conversion to ethyl esters and an estimated cost of the process variables. Fungal biomass of Mucor circinelloides was cultivated in sugarcane molasses media and the obtained oleaginous cells were used as the source of acylglycerols and free fatty acids for the trans/esterification reactions in a pressurized stainless-steel reactor at 200 °C for 6 h. Our results demonstrate that the effects of the two factors analyzed were significant, with an indication that increases in the molar ratio and catalyst favor the reaction yield. In the reaction system, a molar ratio of 120:1 (ethanol: oil) and 15 wt% of catalyst yielded 96.6% of ester content, which meets the minimum limit established by the international standards. Production costs were estimated in function of ethanol and catalyst price and indicated the selected parameters reflected the adequate configuration to reach the stablished minimum ester content.
publishDate 2021
dc.date.none.fl_str_mv 2021-06-25T10:29:49Z
2021-06-25T10:29:49Z
2021-09-15
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.fuel.2021.120968
Fuel, v. 300.
0016-2361
http://hdl.handle.net/11449/206300
10.1016/j.fuel.2021.120968
2-s2.0-85105282710
url http://dx.doi.org/10.1016/j.fuel.2021.120968
http://hdl.handle.net/11449/206300
identifier_str_mv Fuel, v. 300.
0016-2361
10.1016/j.fuel.2021.120968
2-s2.0-85105282710
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv Fuel
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.source.none.fl_str_mv Scopus
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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