Polyhydroxyalkanoates production from ethanol- and lactate-rich fermentate of confectionary industry effluents

Polyhydroxyalkanoate (PHA) production has been the focus of considerable research to increase productivities and reduce production costs. In this study, a fermented confectionary industry wastewater was used as feedstock for mixed microbial culture PHA production. The feedstock was dominated by lact...

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Published inInternational journal of biological macromolecules Vol. 229; pp. 713 - 723
Main Authors Rangel, Catarina, Carvalho, Gilda, Oehmen, Adrian, Frison, Nicola, Lourenço, Nídia D., Reis, Maria A.M.
Format Journal Article
LanguageEnglish
Published Netherlands Elsevier B.V 28.02.2023
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ISSN0141-8130
1879-0003
1879-0003
DOI10.1016/j.ijbiomac.2022.12.268

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Abstract Polyhydroxyalkanoate (PHA) production has been the focus of considerable research to increase productivities and reduce production costs. In this study, a fermented confectionary industry wastewater was used as feedstock for mixed microbial culture PHA production. The feedstock was dominated by lactate and ethanol (60–90 % of all soluble fermentation products). The culture selection reactor was inoculated with municipal activated sludge and was operated at an organic loading rate (OLR) of 100 Cmmol·L−1·d−1, achieving a robust PHA-accumulating enrichment, which produced up to 52.6 ± 0.4 wt% of PHA in accumulation assays. An OLR increase in the culture selection stage to 150 Cmmol·L−1·d−1 led to a PHA content of 59.1 ± 0.6, a yield of 0.93 ± 0.01 Cmol-PHA·Cmol-S−1 and a productivity of 0.93 ± 0.01 g-PHA L−1·h−1. A correlation analysis of the impact of ethanol concentrations from 3.19 to 20.3 Cmmol·L−1 in the reactor showed that ethanol inhibited PHA production rate and yield and the consumption of other carbon sources available. Microbial community analysis revealed the increase of Amaricoccus genus during the bioreactor operation time, a known PHA accumulator. The produced polymer was poly(3-hydroxybutyrate) with an average molecular weight of 4.3 × 105 Da and a polydispersity index of 1.88. [Display omitted] •Fermented confectionary industry effluent was high in ethanol and acetate.•A robust PHA accumulating mixed culture was selected using the fermented feedstock.•The culture was able to adapt to significant shifts in feedstock composition.•Multiparametric correlation analysis evidenced ethanol inhibition in PHA production.•Competitive PHA productivity/yield attained despite high lactate/ethanol levels.
AbstractList Polyhydroxyalkanoate (PHA) production has been the focus of considerable research to increase productivities and reduce production costs. In this study, a fermented confectionary industry wastewater was used as feedstock for mixed microbial culture PHA production. The feedstock was dominated by lactate and ethanol (60-90 % of all soluble fermentation products). The culture selection reactor was inoculated with municipal activated sludge and was operated at an organic loading rate (OLR) of 100 Cmmol·L ·d , achieving a robust PHA-accumulating enrichment, which produced up to 52.6 ± 0.4 wt% of PHA in accumulation assays. An OLR increase in the culture selection stage to 150 Cmmol·L ·d led to a PHA content of 59.1 ± 0.6, a yield of 0.93 ± 0.01 Cmol-PHA·Cmol-S and a productivity of 0.93 ± 0.01 g-PHA L ·h . A correlation analysis of the impact of ethanol concentrations from 3.19 to 20.3 Cmmol·L in the reactor showed that ethanol inhibited PHA production rate and yield and the consumption of other carbon sources available. Microbial community analysis revealed the increase of Amaricoccus genus during the bioreactor operation time, a known PHA accumulator. The produced polymer was poly(3-hydroxybutyrate) with an average molecular weight of 4.3 × 10  Da and a polydispersity index of 1.88.
Polyhydroxyalkanoate (PHA) production has been the focus of considerable research to increase productivities and reduce production costs. In this study, a fermented confectionary industry wastewater was used as feedstock for mixed microbial culture PHA production. The feedstock was dominated by lactate and ethanol (60–90 % of all soluble fermentation products). The culture selection reactor was inoculated with municipal activated sludge and was operated at an organic loading rate (OLR) of 100 Cmmol·L−1·d−1, achieving a robust PHA-accumulating enrichment, which produced up to 52.6 ± 0.4 wt% of PHA in accumulation assays. An OLR increase in the culture selection stage to 150 Cmmol·L−1·d−1 led to a PHA content of 59.1 ± 0.6, a yield of 0.93 ± 0.01 Cmol-PHA·Cmol-S−1 and a productivity of 0.93 ± 0.01 g-PHA L−1·h−1. A correlation analysis of the impact of ethanol concentrations from 3.19 to 20.3 Cmmol·L−1 in the reactor showed that ethanol inhibited PHA production rate and yield and the consumption of other carbon sources available. Microbial community analysis revealed the increase of Amaricoccus genus during the bioreactor operation time, a known PHA accumulator. The produced polymer was poly(3-hydroxybutyrate) with an average molecular weight of 4.3 × 105 Da and a polydispersity index of 1.88. [Display omitted] •Fermented confectionary industry effluent was high in ethanol and acetate.•A robust PHA accumulating mixed culture was selected using the fermented feedstock.•The culture was able to adapt to significant shifts in feedstock composition.•Multiparametric correlation analysis evidenced ethanol inhibition in PHA production.•Competitive PHA productivity/yield attained despite high lactate/ethanol levels.
Polyhydroxyalkanoate (PHA) production has been the focus of considerable research to increase productivities and reduce production costs. In this study, a fermented confectionary industry wastewater was used as feedstock for mixed microbial culture PHA production. The feedstock was dominated by lactate and ethanol (60–90 % of all soluble fermentation products). The culture selection reactor was inoculated with municipal activated sludge and was operated at an organic loading rate (OLR) of 100 Cmmol·L⁻¹·d⁻¹, achieving a robust PHA-accumulating enrichment, which produced up to 52.6 ± 0.4 wt% of PHA in accumulation assays. An OLR increase in the culture selection stage to 150 Cmmol·L⁻¹·d⁻¹ led to a PHA content of 59.1 ± 0.6, a yield of 0.93 ± 0.01 Cmol-PHA·Cmol-S⁻¹ and a productivity of 0.93 ± 0.01 g-PHA L⁻¹·h⁻¹. A correlation analysis of the impact of ethanol concentrations from 3.19 to 20.3 Cmmol·L⁻¹ in the reactor showed that ethanol inhibited PHA production rate and yield and the consumption of other carbon sources available. Microbial community analysis revealed the increase of Amaricoccus genus during the bioreactor operation time, a known PHA accumulator. The produced polymer was poly(3-hydroxybutyrate) with an average molecular weight of 4.3 × 10⁵ Da and a polydispersity index of 1.88.
Polyhydroxyalkanoate (PHA) production has been the focus of considerable research to increase productivities and reduce production costs. In this study, a fermented confectionary industry wastewater was used as feedstock for mixed microbial culture PHA production. The feedstock was dominated by lactate and ethanol (60-90 % of all soluble fermentation products). The culture selection reactor was inoculated with municipal activated sludge and was operated at an organic loading rate (OLR) of 100 Cmmol·L-1·d-1, achieving a robust PHA-accumulating enrichment, which produced up to 52.6 ± 0.4 wt% of PHA in accumulation assays. An OLR increase in the culture selection stage to 150 Cmmol·L-1·d-1 led to a PHA content of 59.1 ± 0.6, a yield of 0.93 ± 0.01 Cmol-PHA·Cmol-S-1 and a productivity of 0.93 ± 0.01 g-PHA L-1·h-1. A correlation analysis of the impact of ethanol concentrations from 3.19 to 20.3 Cmmol·L-1 in the reactor showed that ethanol inhibited PHA production rate and yield and the consumption of other carbon sources available. Microbial community analysis revealed the increase of Amaricoccus genus during the bioreactor operation time, a known PHA accumulator. The produced polymer was poly(3-hydroxybutyrate) with an average molecular weight of 4.3 × 105 Da and a polydispersity index of 1.88.Polyhydroxyalkanoate (PHA) production has been the focus of considerable research to increase productivities and reduce production costs. In this study, a fermented confectionary industry wastewater was used as feedstock for mixed microbial culture PHA production. The feedstock was dominated by lactate and ethanol (60-90 % of all soluble fermentation products). The culture selection reactor was inoculated with municipal activated sludge and was operated at an organic loading rate (OLR) of 100 Cmmol·L-1·d-1, achieving a robust PHA-accumulating enrichment, which produced up to 52.6 ± 0.4 wt% of PHA in accumulation assays. An OLR increase in the culture selection stage to 150 Cmmol·L-1·d-1 led to a PHA content of 59.1 ± 0.6, a yield of 0.93 ± 0.01 Cmol-PHA·Cmol-S-1 and a productivity of 0.93 ± 0.01 g-PHA L-1·h-1. A correlation analysis of the impact of ethanol concentrations from 3.19 to 20.3 Cmmol·L-1 in the reactor showed that ethanol inhibited PHA production rate and yield and the consumption of other carbon sources available. Microbial community analysis revealed the increase of Amaricoccus genus during the bioreactor operation time, a known PHA accumulator. The produced polymer was poly(3-hydroxybutyrate) with an average molecular weight of 4.3 × 105 Da and a polydispersity index of 1.88.
Author Rangel, Catarina
Oehmen, Adrian
Carvalho, Gilda
Reis, Maria A.M.
Lourenço, Nídia D.
Frison, Nicola
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Keywords Polyhydroxyalkanoate (PHA)
Lactate
Ethanol
Language English
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Snippet Polyhydroxyalkanoate (PHA) production has been the focus of considerable research to increase productivities and reduce production costs. In this study, a...
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SubjectTerms activated sludge
Amaricoccus
Bioreactors
carbon
confectionery industry
Ethanol
feedstocks
Fermentation
genus
industrial wastewater
Lactate
Lactic Acid
microbial communities
microbial culture
molecular weight
Polyhydroxyalkanoate (PHA)
Polyhydroxyalkanoates
Sewage
Wastewater
Title Polyhydroxyalkanoates production from ethanol- and lactate-rich fermentate of confectionary industry effluents
URI https://dx.doi.org/10.1016/j.ijbiomac.2022.12.268
https://www.ncbi.nlm.nih.gov/pubmed/36587645
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https://www.proquest.com/docview/3153777247
Volume 229
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