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 in | International journal of biological macromolecules Vol. 229; pp. 713 - 723 |
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Main Authors | , , , , , |
Format | Journal Article |
Language | English |
Published |
Netherlands
Elsevier B.V
28.02.2023
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Subjects | |
Online Access | Get full text |
ISSN | 0141-8130 1879-0003 1879-0003 |
DOI | 10.1016/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. |
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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 |
Author_xml | – sequence: 1 givenname: Catarina surname: Rangel fullname: Rangel, Catarina organization: Associate Laboratory i4HB–Institute for Health and Bioeconomy, NOVA School of Science and Technology, NOVA University Lisbon, 2829-516 Caparica, Portugal – sequence: 2 givenname: Gilda surname: Carvalho fullname: Carvalho, Gilda email: g.carvalho@uq.edu.au organization: Australian Centre for Water and Environmental Biotechnology (ACWEB, formerly AWMC), The University of Queensland, St Lucia, Queensland 4072, Australia – sequence: 3 givenname: Adrian surname: Oehmen fullname: Oehmen, Adrian organization: School of Chemical Engineering, The University of Queensland, St Lucia, Queensland 4072, Australia – sequence: 4 givenname: Nicola surname: Frison fullname: Frison, Nicola organization: University of Verona, Department of Biotechnology, Strada Le Grazie, 15, 37134 Verona, Italy – sequence: 5 givenname: Nídia D. surname: Lourenço fullname: Lourenço, Nídia D. email: nidia.lourenco@fct.unl.pt organization: Associate Laboratory i4HB–Institute for Health and Bioeconomy, NOVA School of Science and Technology, NOVA University Lisbon, 2829-516 Caparica, Portugal – sequence: 6 givenname: Maria A.M. surname: Reis fullname: Reis, Maria A.M. organization: Associate Laboratory i4HB–Institute for Health and Bioeconomy, NOVA School of Science and Technology, NOVA University Lisbon, 2829-516 Caparica, Portugal |
BackLink | https://www.ncbi.nlm.nih.gov/pubmed/36587645$$D View this record in MEDLINE/PubMed |
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Keywords | Polyhydroxyalkanoate (PHA) Lactate Ethanol |
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Title | Polyhydroxyalkanoates production from ethanol- and lactate-rich fermentate of confectionary industry effluents |
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