Enhanced Fermentative Hydrogen Production from Food Waste in Continuous Reactor after Butyric Acid Treatment

End-product accumulation during dark fermentation leads to process instability and hydrogen production inhibition. To overcome this constraint, microbial community adaptation to butyric acid can induce acid tolerance and thus enhance the hydrogen yields; however, adaptation and selection of appropri...

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Main Authors: Marie Céline Noguer, Jose Antonio Magdalena, Nicolas Bernet, Renaud Escudié, Eric Trably
Format: Article
Language:English
Published: MDPI AG 2022-05-01
Series:Energies
Subjects:
Online Access:https://www.mdpi.com/1996-1073/15/11/4048
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author Marie Céline Noguer
Jose Antonio Magdalena
Nicolas Bernet
Renaud Escudié
Eric Trably
author_facet Marie Céline Noguer
Jose Antonio Magdalena
Nicolas Bernet
Renaud Escudié
Eric Trably
author_sort Marie Céline Noguer
collection DOAJ
description End-product accumulation during dark fermentation leads to process instability and hydrogen production inhibition. To overcome this constraint, microbial community adaptation to butyric acid can induce acid tolerance and thus enhance the hydrogen yields; however, adaptation and selection of appropriate microbial communities remains uncertain when dealing with complex substrates in a continuous fermentation mode. To address this question, a reactor fed in continuous mode with food waste (organic loading rate of 60 gVS·L·d<sup>−1</sup>; 12 h hydraulic retention time) was first stressed for 48 h with increasing concentrations of butyric acid (up to 8.7 g·L<sup>−1</sup>). Performances were compared with a control reactor (unstressed) for 13 days. During 6 days in a steady-state, the pre-stressed reactor produced 2.2 ± 0.2 LH<sub>2</sub>·L·d<sup>−1</sup>, which was 48% higher than in the control reactor (1.5 ± 0.2 LH<sub>2</sub>·L·d<sup>−1</sup>). The pretreatment also affected the metabolites’ distribution. The pre-stressed reactor presented a higher production of butyric acid (+44%) achieving up to 3.8 ± 0.3 g·L<sup>−1</sup>, a lower production of lactic acid (−56%), and an enhancement of substrate conversion (+9%). The performance improvement was attributed to the promotion of <i>Clostridium guangxiense</i>, a hydrogen -producer, with a relative abundance increasing from 22% in the unstressed reactor to 52% in the stressed reactor.
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spelling doaj.art-742cb3db803b407aa0e7b75e0c8ab9742023-11-23T13:59:27ZengMDPI AGEnergies1996-10732022-05-011511404810.3390/en15114048Enhanced Fermentative Hydrogen Production from Food Waste in Continuous Reactor after Butyric Acid TreatmentMarie Céline Noguer0Jose Antonio Magdalena1Nicolas Bernet2Renaud Escudié3Eric Trably4INRAE, University of Montpellier, LBE, 102 Avenue des Etangs, 11100 Narbonne, FranceINRAE, University of Montpellier, LBE, 102 Avenue des Etangs, 11100 Narbonne, FranceINRAE, University of Montpellier, LBE, 102 Avenue des Etangs, 11100 Narbonne, FranceINRAE, University of Montpellier, LBE, 102 Avenue des Etangs, 11100 Narbonne, FranceINRAE, University of Montpellier, LBE, 102 Avenue des Etangs, 11100 Narbonne, FranceEnd-product accumulation during dark fermentation leads to process instability and hydrogen production inhibition. To overcome this constraint, microbial community adaptation to butyric acid can induce acid tolerance and thus enhance the hydrogen yields; however, adaptation and selection of appropriate microbial communities remains uncertain when dealing with complex substrates in a continuous fermentation mode. To address this question, a reactor fed in continuous mode with food waste (organic loading rate of 60 gVS·L·d<sup>−1</sup>; 12 h hydraulic retention time) was first stressed for 48 h with increasing concentrations of butyric acid (up to 8.7 g·L<sup>−1</sup>). Performances were compared with a control reactor (unstressed) for 13 days. During 6 days in a steady-state, the pre-stressed reactor produced 2.2 ± 0.2 LH<sub>2</sub>·L·d<sup>−1</sup>, which was 48% higher than in the control reactor (1.5 ± 0.2 LH<sub>2</sub>·L·d<sup>−1</sup>). The pretreatment also affected the metabolites’ distribution. The pre-stressed reactor presented a higher production of butyric acid (+44%) achieving up to 3.8 ± 0.3 g·L<sup>−1</sup>, a lower production of lactic acid (−56%), and an enhancement of substrate conversion (+9%). The performance improvement was attributed to the promotion of <i>Clostridium guangxiense</i>, a hydrogen -producer, with a relative abundance increasing from 22% in the unstressed reactor to 52% in the stressed reactor.https://www.mdpi.com/1996-1073/15/11/4048biohydrogenbutyric aciddark fermentationinhibitionmicrobial communitiesstart-up
spellingShingle Marie Céline Noguer
Jose Antonio Magdalena
Nicolas Bernet
Renaud Escudié
Eric Trably
Enhanced Fermentative Hydrogen Production from Food Waste in Continuous Reactor after Butyric Acid Treatment
Energies
biohydrogen
butyric acid
dark fermentation
inhibition
microbial communities
start-up
title Enhanced Fermentative Hydrogen Production from Food Waste in Continuous Reactor after Butyric Acid Treatment
title_full Enhanced Fermentative Hydrogen Production from Food Waste in Continuous Reactor after Butyric Acid Treatment
title_fullStr Enhanced Fermentative Hydrogen Production from Food Waste in Continuous Reactor after Butyric Acid Treatment
title_full_unstemmed Enhanced Fermentative Hydrogen Production from Food Waste in Continuous Reactor after Butyric Acid Treatment
title_short Enhanced Fermentative Hydrogen Production from Food Waste in Continuous Reactor after Butyric Acid Treatment
title_sort enhanced fermentative hydrogen production from food waste in continuous reactor after butyric acid treatment
topic biohydrogen
butyric acid
dark fermentation
inhibition
microbial communities
start-up
url https://www.mdpi.com/1996-1073/15/11/4048
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