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Butanol as a major product during ethanol and acetate chain elongation

Chain elongation is a relevant bioprocess in support of a circular economy as it can use a variety of organic feedstocks for production of valuable short and medium chain carboxylates, such as butyrate (C4), caproate (C6), and caprylate (C8). Alcohols, including the biofuel, butanol (C4), can also b...

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Autores principales: Robles, Aide, Sundar, Skanda Vishnu, Mohana Rangan, Srivatsan, Delgado, Anca G.
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Frontiers Media S.A. 2023
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10233103/
https://www.ncbi.nlm.nih.gov/pubmed/37274171
http://dx.doi.org/10.3389/fbioe.2023.1181983
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author Robles, Aide
Sundar, Skanda Vishnu
Mohana Rangan, Srivatsan
Delgado, Anca G.
author_facet Robles, Aide
Sundar, Skanda Vishnu
Mohana Rangan, Srivatsan
Delgado, Anca G.
author_sort Robles, Aide
collection PubMed
description Chain elongation is a relevant bioprocess in support of a circular economy as it can use a variety of organic feedstocks for production of valuable short and medium chain carboxylates, such as butyrate (C4), caproate (C6), and caprylate (C8). Alcohols, including the biofuel, butanol (C4), can also be generated in chain elongation but the bioreactor conditions that favor butanol production are mainly unknown. In this study we investigated production of butanol (and its precursor butyrate) during ethanol and acetate chain elongation. We used semi-batch bioreactors (0.16 L serum bottles) fed with a range of ethanol concentrations (100–800 mM C), a constant concentration of acetate (50 mM C), and an initial total gas pressure of ∼112 kPa. We showed that the butanol concentration was positively correlated with the ethanol concentration provided (up to 400 mM C ethanol) and to chain elongation activity, which produced H(2) and further increased the total gas pressure. In bioreactors fed with 400 mM C ethanol and 50 mM C acetate, a concentration of 114.96 ± 9.26 mM C butanol (∼2.13 g L(−1)) was achieved after five semi-batch cycles at a total pressure of ∼170 kPa and H(2) partial pressure of ∼67 kPa. Bioreactors with 400 mM C ethanol and 50 mM C acetate also yielded a butanol to butyrate molar ratio of 1:1. At the beginning of cycle 8, the total gas pressure was intentionally decreased to ∼112 kPa to test the dependency of butanol production on total pressure and H(2) partial pressure. The reduction in total pressure decreased the molar ratio of butanol to butyrate to 1:2 and jolted H(2) production out of an apparent stall. Clostridium kluyveri (previously shown to produce butyrate and butanol) and Alistipes (previously linked with butyrate production) were abundant amplicon sequence variants in the bioreactors during the experimental phases, suggesting the microbiome was resilient against changes in bioreactor conditions. The results from this study clearly demonstrate the potential of ethanol and acetate-based chain elongation to yield butanol as a major product. This study also supports the dependency of butanol production on limiting acetate and on high total gas and H(2) partial pressures.
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spelling pubmed-102331032023-06-02 Butanol as a major product during ethanol and acetate chain elongation Robles, Aide Sundar, Skanda Vishnu Mohana Rangan, Srivatsan Delgado, Anca G. Front Bioeng Biotechnol Bioengineering and Biotechnology Chain elongation is a relevant bioprocess in support of a circular economy as it can use a variety of organic feedstocks for production of valuable short and medium chain carboxylates, such as butyrate (C4), caproate (C6), and caprylate (C8). Alcohols, including the biofuel, butanol (C4), can also be generated in chain elongation but the bioreactor conditions that favor butanol production are mainly unknown. In this study we investigated production of butanol (and its precursor butyrate) during ethanol and acetate chain elongation. We used semi-batch bioreactors (0.16 L serum bottles) fed with a range of ethanol concentrations (100–800 mM C), a constant concentration of acetate (50 mM C), and an initial total gas pressure of ∼112 kPa. We showed that the butanol concentration was positively correlated with the ethanol concentration provided (up to 400 mM C ethanol) and to chain elongation activity, which produced H(2) and further increased the total gas pressure. In bioreactors fed with 400 mM C ethanol and 50 mM C acetate, a concentration of 114.96 ± 9.26 mM C butanol (∼2.13 g L(−1)) was achieved after five semi-batch cycles at a total pressure of ∼170 kPa and H(2) partial pressure of ∼67 kPa. Bioreactors with 400 mM C ethanol and 50 mM C acetate also yielded a butanol to butyrate molar ratio of 1:1. At the beginning of cycle 8, the total gas pressure was intentionally decreased to ∼112 kPa to test the dependency of butanol production on total pressure and H(2) partial pressure. The reduction in total pressure decreased the molar ratio of butanol to butyrate to 1:2 and jolted H(2) production out of an apparent stall. Clostridium kluyveri (previously shown to produce butyrate and butanol) and Alistipes (previously linked with butyrate production) were abundant amplicon sequence variants in the bioreactors during the experimental phases, suggesting the microbiome was resilient against changes in bioreactor conditions. The results from this study clearly demonstrate the potential of ethanol and acetate-based chain elongation to yield butanol as a major product. This study also supports the dependency of butanol production on limiting acetate and on high total gas and H(2) partial pressures. Frontiers Media S.A. 2023-05-18 /pmc/articles/PMC10233103/ /pubmed/37274171 http://dx.doi.org/10.3389/fbioe.2023.1181983 Text en Copyright © 2023 Robles, Sundar, Mohana Rangan and Delgado. https://creativecommons.org/licenses/by/4.0/This is an open-access article distributed under the terms of the Creative Commons Attribution License (CC BY). The use, distribution or reproduction in other forums is permitted, provided the original author(s) and the copyright owner(s) are credited and that the original publication in this journal is cited, in accordance with accepted academic practice. No use, distribution or reproduction is permitted which does not comply with these terms.
spellingShingle Bioengineering and Biotechnology
Robles, Aide
Sundar, Skanda Vishnu
Mohana Rangan, Srivatsan
Delgado, Anca G.
Butanol as a major product during ethanol and acetate chain elongation
title Butanol as a major product during ethanol and acetate chain elongation
title_full Butanol as a major product during ethanol and acetate chain elongation
title_fullStr Butanol as a major product during ethanol and acetate chain elongation
title_full_unstemmed Butanol as a major product during ethanol and acetate chain elongation
title_short Butanol as a major product during ethanol and acetate chain elongation
title_sort butanol as a major product during ethanol and acetate chain elongation
topic Bioengineering and Biotechnology
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10233103/
https://www.ncbi.nlm.nih.gov/pubmed/37274171
http://dx.doi.org/10.3389/fbioe.2023.1181983
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AT delgadoancag butanolasamajorproductduringethanolandacetatechainelongation