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CO2 supply is a powerful tool to control homoacetogenesis, chain elongation and solventogenesis in ethanol and carboxylate fed reactor microbiomes
Anaerobic fermentation technology enables the production of medium chain carboxylates and alcohols through microbial chain elongation. This involves steering reactor microbiomes to yield desired products, with CO 2 supply playing a crucial role in controlling ethanol-based chain elongation and facil...
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Published in: | Frontiers in bioengineering and biotechnology 2024-04, Vol.12, p.1329288-1329288 |
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description | Anaerobic fermentation technology enables the production of medium chain carboxylates and alcohols through microbial chain elongation. This involves steering reactor microbiomes to yield desired products, with CO
2
supply playing a crucial role in controlling ethanol-based chain elongation and facilitating various bioprocesses simultaneously. In the absence of CO
2
supply (Phase I), chain elongation predominantly led to n-caproate with a high selectivity of 96 Cmol%, albeit leaving approximately 80% of ethanol unconverted. During this phase,
C. kluyveri
and
Proteiniphilum
-related species dominated the reactors. In Phase II, with low CO
2
input (2.0 NmL L
−1
min
−1
), formation of n-butyrate, butanol, and hexanol was stimulated. Increasing CO
2
doses in Phase III (6 NmL L
−1
min
−1
) led to CO
2
utilization via homoacetogenesis, coinciding with the enrichment of
Clostridium luticellarii
, a bacterium that can use CO
2
as an electron acceptor. Lowering CO
2
dose to 0.5 NmL L
−1
min
−1
led to a shift in microbiome composition, diminishing the dominance of
C. luticellarii
while increasing
C. kluyveri
abundance. Additionally, other
Clostridia
,
Proteiniphilum
, and
Lactobacillus sakei
-related species became prevalent. This decrease in CO
2
load from 6 to 0.5 NmL L
−1
min
−1
minimized excessive ethanol oxidation from 30%–50% to 0%–3%, restoring a microbiome favoring net n-butyrate consumption and n-caproate production. The decreased ethanol oxidation coincided with the resurgence of hydrogen formation at partial pressures above 1%. High concentrations of butyrate, caproate, and ethanol in the reactor, along with low acetate concentration, promoted the formation of butanol and hexanol. It is evident that CO
2
supply is indispensable for controlling chain elongation in an open culture and it can be harnessed to stimulate higher alcohol formation or induce CO
2
utilization as an electron acceptor. |
doi_str_mv | 10.3389/fbioe.2024.1329288 |
format | article |
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2
supply playing a crucial role in controlling ethanol-based chain elongation and facilitating various bioprocesses simultaneously. In the absence of CO
2
supply (Phase I), chain elongation predominantly led to n-caproate with a high selectivity of 96 Cmol%, albeit leaving approximately 80% of ethanol unconverted. During this phase,
C. kluyveri
and
Proteiniphilum
-related species dominated the reactors. In Phase II, with low CO
2
input (2.0 NmL L
−1
min
−1
), formation of n-butyrate, butanol, and hexanol was stimulated. Increasing CO
2
doses in Phase III (6 NmL L
−1
min
−1
) led to CO
2
utilization via homoacetogenesis, coinciding with the enrichment of
Clostridium luticellarii
, a bacterium that can use CO
2
as an electron acceptor. Lowering CO
2
dose to 0.5 NmL L
−1
min
−1
led to a shift in microbiome composition, diminishing the dominance of
C. luticellarii
while increasing
C. kluyveri
abundance. Additionally, other
Clostridia
,
Proteiniphilum
, and
Lactobacillus sakei
-related species became prevalent. This decrease in CO
2
load from 6 to 0.5 NmL L
−1
min
−1
minimized excessive ethanol oxidation from 30%–50% to 0%–3%, restoring a microbiome favoring net n-butyrate consumption and n-caproate production. The decreased ethanol oxidation coincided with the resurgence of hydrogen formation at partial pressures above 1%. High concentrations of butyrate, caproate, and ethanol in the reactor, along with low acetate concentration, promoted the formation of butanol and hexanol. It is evident that CO
2
supply is indispensable for controlling chain elongation in an open culture and it can be harnessed to stimulate higher alcohol formation or induce CO
2
utilization as an electron acceptor.</description><identifier>ISSN: 2296-4185</identifier><identifier>EISSN: 2296-4185</identifier><identifier>DOI: 10.3389/fbioe.2024.1329288</identifier><language>eng</language><publisher>Frontiers Media S.A</publisher><subject>acetogenesis ; Bioengineering and Biotechnology ; chain elongation ; CO2 ; ethanol ; reduction ; solventogenesis</subject><ispartof>Frontiers in bioengineering and biotechnology, 2024-04, Vol.12, p.1329288-1329288</ispartof><rights>Copyright © 2024 de Leeuw, van Willigen, Vrauwdeunt and Strik. 2024 de Leeuw, van Willigen, Vrauwdeunt and Strik</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><cites>FETCH-LOGICAL-c397t-71b895942063633819a9bfb68f7ce764bc06d3a9aaac8e8ee7da49dc4a2cc0213</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://www.ncbi.nlm.nih.gov/pmc/articles/PMC11076876/pdf/$$EPDF$$P50$$Gpubmedcentral$$Hfree_for_read</linktopdf><linktohtml>$$Uhttps://www.ncbi.nlm.nih.gov/pmc/articles/PMC11076876/$$EHTML$$P50$$Gpubmedcentral$$Hfree_for_read</linktohtml><link.rule.ids>230,314,727,780,784,885,27924,27925,53791,53793</link.rule.ids></links><search><creatorcontrib>de Leeuw, Kasper D.</creatorcontrib><creatorcontrib>van Willigen, Marius J. W.</creatorcontrib><creatorcontrib>Vrauwdeunt, Ton</creatorcontrib><creatorcontrib>Strik, David P. P. T. B.</creatorcontrib><title>CO2 supply is a powerful tool to control homoacetogenesis, chain elongation and solventogenesis in ethanol and carboxylate fed reactor microbiomes</title><title>Frontiers in bioengineering and biotechnology</title><description>Anaerobic fermentation technology enables the production of medium chain carboxylates and alcohols through microbial chain elongation. This involves steering reactor microbiomes to yield desired products, with CO
2
supply playing a crucial role in controlling ethanol-based chain elongation and facilitating various bioprocesses simultaneously. In the absence of CO
2
supply (Phase I), chain elongation predominantly led to n-caproate with a high selectivity of 96 Cmol%, albeit leaving approximately 80% of ethanol unconverted. During this phase,
C. kluyveri
and
Proteiniphilum
-related species dominated the reactors. In Phase II, with low CO
2
input (2.0 NmL L
−1
min
−1
), formation of n-butyrate, butanol, and hexanol was stimulated. Increasing CO
2
doses in Phase III (6 NmL L
−1
min
−1
) led to CO
2
utilization via homoacetogenesis, coinciding with the enrichment of
Clostridium luticellarii
, a bacterium that can use CO
2
as an electron acceptor. Lowering CO
2
dose to 0.5 NmL L
−1
min
−1
led to a shift in microbiome composition, diminishing the dominance of
C. luticellarii
while increasing
C. kluyveri
abundance. Additionally, other
Clostridia
,
Proteiniphilum
, and
Lactobacillus sakei
-related species became prevalent. This decrease in CO
2
load from 6 to 0.5 NmL L
−1
min
−1
minimized excessive ethanol oxidation from 30%–50% to 0%–3%, restoring a microbiome favoring net n-butyrate consumption and n-caproate production. The decreased ethanol oxidation coincided with the resurgence of hydrogen formation at partial pressures above 1%. High concentrations of butyrate, caproate, and ethanol in the reactor, along with low acetate concentration, promoted the formation of butanol and hexanol. It is evident that CO
2
supply is indispensable for controlling chain elongation in an open culture and it can be harnessed to stimulate higher alcohol formation or induce CO
2
utilization as an electron acceptor.</description><subject>acetogenesis</subject><subject>Bioengineering and Biotechnology</subject><subject>chain elongation</subject><subject>CO2</subject><subject>ethanol</subject><subject>reduction</subject><subject>solventogenesis</subject><issn>2296-4185</issn><issn>2296-4185</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2024</creationdate><recordtype>article</recordtype><sourceid>DOA</sourceid><recordid>eNpVks1q3DAUhU1poSHJC3SlZRedqX5sS1qVMvQnEMimXYsr6XpGwbZcyU47r5EnrpwZQrKRDvcePqHDqaoPjG6FUPpzZ0PELae83jLBNVfqTXXBuW43NVPN2xf6fXWd8z2llPFGNopfVI-7O07yMk39kYRMgEzxL6Zu6ckc43oQF8c5FXmIQwSHc9zjiDnkT8QdIIwE-zjuYQ5xJDB6kmP_gOOzi6yO-QBjIaxrB8nGf8ceZiQdepIQ3BwTGYJLsfxjwHxVveugz3h9vi-r39-__dr93Nze_bjZfb3dOKHlvJHMKt3omtNWtCUHpkHbzraqkw5lW1tHWy9AA4BTqBClh1p7VwN3jnImLqubE9dHuDdTCgOko4kQzNMgpr2BNAfXoxFcKt-oprFdW3uLRXHtKevKwHq0hfXlxJoWO6B3JYEE_Svo680YDmYfHwxjVLZKtoXw8UxI8c-CeTZDyA77HkaMSzaCNoIJ2TS0WPnJWiLLOWH3_A6jZm2EeWqEWRthzo0Q_wEWPK_A</recordid><startdate>20240424</startdate><enddate>20240424</enddate><creator>de Leeuw, Kasper D.</creator><creator>van Willigen, Marius J. W.</creator><creator>Vrauwdeunt, Ton</creator><creator>Strik, David P. P. T. B.</creator><general>Frontiers Media S.A</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7X8</scope><scope>5PM</scope><scope>DOA</scope></search><sort><creationdate>20240424</creationdate><title>CO2 supply is a powerful tool to control homoacetogenesis, chain elongation and solventogenesis in ethanol and carboxylate fed reactor microbiomes</title><author>de Leeuw, Kasper D. ; van Willigen, Marius J. W. ; Vrauwdeunt, Ton ; Strik, David P. P. T. B.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c397t-71b895942063633819a9bfb68f7ce764bc06d3a9aaac8e8ee7da49dc4a2cc0213</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2024</creationdate><topic>acetogenesis</topic><topic>Bioengineering and Biotechnology</topic><topic>chain elongation</topic><topic>CO2</topic><topic>ethanol</topic><topic>reduction</topic><topic>solventogenesis</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>de Leeuw, Kasper D.</creatorcontrib><creatorcontrib>van Willigen, Marius J. W.</creatorcontrib><creatorcontrib>Vrauwdeunt, Ton</creatorcontrib><creatorcontrib>Strik, David P. P. T. B.</creatorcontrib><collection>CrossRef</collection><collection>MEDLINE - Academic</collection><collection>PubMed Central (Full Participant titles)</collection><collection>DOAJ Directory of Open Access Journals</collection><jtitle>Frontiers in bioengineering and biotechnology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>de Leeuw, Kasper D.</au><au>van Willigen, Marius J. W.</au><au>Vrauwdeunt, Ton</au><au>Strik, David P. P. T. B.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>CO2 supply is a powerful tool to control homoacetogenesis, chain elongation and solventogenesis in ethanol and carboxylate fed reactor microbiomes</atitle><jtitle>Frontiers in bioengineering and biotechnology</jtitle><date>2024-04-24</date><risdate>2024</risdate><volume>12</volume><spage>1329288</spage><epage>1329288</epage><pages>1329288-1329288</pages><issn>2296-4185</issn><eissn>2296-4185</eissn><abstract>Anaerobic fermentation technology enables the production of medium chain carboxylates and alcohols through microbial chain elongation. This involves steering reactor microbiomes to yield desired products, with CO
2
supply playing a crucial role in controlling ethanol-based chain elongation and facilitating various bioprocesses simultaneously. In the absence of CO
2
supply (Phase I), chain elongation predominantly led to n-caproate with a high selectivity of 96 Cmol%, albeit leaving approximately 80% of ethanol unconverted. During this phase,
C. kluyveri
and
Proteiniphilum
-related species dominated the reactors. In Phase II, with low CO
2
input (2.0 NmL L
−1
min
−1
), formation of n-butyrate, butanol, and hexanol was stimulated. Increasing CO
2
doses in Phase III (6 NmL L
−1
min
−1
) led to CO
2
utilization via homoacetogenesis, coinciding with the enrichment of
Clostridium luticellarii
, a bacterium that can use CO
2
as an electron acceptor. Lowering CO
2
dose to 0.5 NmL L
−1
min
−1
led to a shift in microbiome composition, diminishing the dominance of
C. luticellarii
while increasing
C. kluyveri
abundance. Additionally, other
Clostridia
,
Proteiniphilum
, and
Lactobacillus sakei
-related species became prevalent. This decrease in CO
2
load from 6 to 0.5 NmL L
−1
min
−1
minimized excessive ethanol oxidation from 30%–50% to 0%–3%, restoring a microbiome favoring net n-butyrate consumption and n-caproate production. The decreased ethanol oxidation coincided with the resurgence of hydrogen formation at partial pressures above 1%. High concentrations of butyrate, caproate, and ethanol in the reactor, along with low acetate concentration, promoted the formation of butanol and hexanol. It is evident that CO
2
supply is indispensable for controlling chain elongation in an open culture and it can be harnessed to stimulate higher alcohol formation or induce CO
2
utilization as an electron acceptor.</abstract><pub>Frontiers Media S.A</pub><doi>10.3389/fbioe.2024.1329288</doi><tpages>1</tpages><oa>free_for_read</oa></addata></record> |
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subjects | acetogenesis Bioengineering and Biotechnology chain elongation CO2 ethanol reduction solventogenesis |
title | CO2 supply is a powerful tool to control homoacetogenesis, chain elongation and solventogenesis in ethanol and carboxylate fed reactor microbiomes |
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