Continuous cultivation strategy for yeast industrial wastewater-based polyhydroxyalkanoate production

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  • Indian Institute of Technology Kharagpur (IITKGP)
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Details

OriginalspracheEnglisch
Seiten (von - bis)595-602
Seitenumfang8
FachzeitschriftJournal of Bioscience and Bioengineering
Jahrgang129
Ausgabenummer5
Frühes Online-Datum10 Dez. 2019
PublikationsstatusVeröffentlicht - Mai 2020

Abstract

Polyhydroxyalkanoates (PHAs) present an eco-friendly alternative for conventional plastics. Industrial wastewater from the food industry is a copious source of organic carbon that can be recovered in the form of PHA. However, the wastewater composition varies considerably among the different industries demanding for an industry-specific investigation of the PHA production process. Wastewater from the yeast industry, besides its high concentration in organic carbon, also contains a high ammonium concentration which might decrease the PHA production. Thus, this study aims to investigate PHA production using yeast industry wastewater via an enriched mixed microbial culture (MMC). A less explored cultivation strategy, i.e., continuous cultivation for PHA production was evaluated and compared to the widely used batch cultivation. PHA accumulating MMC was enriched using a sequencing batch reactor (SBR) operated under aerobic dynamic feeding. An MMC dominated by the Thauera species was successfully enriched in the SBR. Experimental results showed that ammonium is indeed required for PHA accumulation and the complete absence of ammonium negatively affects the accumulation process. Using wastewater, batch and continuous feeding strategies, respectively, yielded the PHA accumulation of 72 % and 65 % per dry cell weight. Despite the slightly lower PHA accumulation with continuous cultivation, four times more biomass growth was produced. Consequently, higher theoretical PHA production (270 t/year) can be expected using continuous cultivation in half of the reactor volume (45 m3). Therefore, this study asserts the viability of continuous cultivation as a feasible investigatory tool and PHA production strategy.

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Continuous cultivation strategy for yeast industrial wastewater-based polyhydroxyalkanoate production. / Bhalerao, Aniruddha; Banerjee, Rintu; Nogueira, Regina.
in: Journal of Bioscience and Bioengineering, Jahrgang 129, Nr. 5, 05.2020, S. 595-602.

Publikation: Beitrag in FachzeitschriftArtikelForschungPeer-Review

Bhalerao A, Banerjee R, Nogueira R. Continuous cultivation strategy for yeast industrial wastewater-based polyhydroxyalkanoate production. Journal of Bioscience and Bioengineering. 2020 Mai;129(5):595-602. Epub 2019 Dez 10. doi: 10.1016/j.jbiosc.2019.11.006
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title = "Continuous cultivation strategy for yeast industrial wastewater-based polyhydroxyalkanoate production",
abstract = "Polyhydroxyalkanoates (PHAs) present an eco-friendly alternative for conventional plastics. Industrial wastewater from the food industry is a copious source of organic carbon that can be recovered in the form of PHA. However, the wastewater composition varies considerably among the different industries demanding for an industry-specific investigation of the PHA production process. Wastewater from the yeast industry, besides its high concentration in organic carbon, also contains a high ammonium concentration which might decrease the PHA production. Thus, this study aims to investigate PHA production using yeast industry wastewater via an enriched mixed microbial culture (MMC). A less explored cultivation strategy, i.e., continuous cultivation for PHA production was evaluated and compared to the widely used batch cultivation. PHA accumulating MMC was enriched using a sequencing batch reactor (SBR) operated under aerobic dynamic feeding. An MMC dominated by the Thauera species was successfully enriched in the SBR. Experimental results showed that ammonium is indeed required for PHA accumulation and the complete absence of ammonium negatively affects the accumulation process. Using wastewater, batch and continuous feeding strategies, respectively, yielded the PHA accumulation of 72 % and 65 % per dry cell weight. Despite the slightly lower PHA accumulation with continuous cultivation, four times more biomass growth was produced. Consequently, higher theoretical PHA production (270 t/year) can be expected using continuous cultivation in half of the reactor volume (45 m3). Therefore, this study asserts the viability of continuous cultivation as a feasible investigatory tool and PHA production strategy.",
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Download

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T1 - Continuous cultivation strategy for yeast industrial wastewater-based polyhydroxyalkanoate production

AU - Bhalerao, Aniruddha

AU - Banerjee, Rintu

AU - Nogueira, Regina

N1 - Funding Information: We acknowledge the Deutscher Akademischer Austauschdienst (DAAD) model Indian Institute of Technology (IIT) Master Sandwich Program scholarships for Master students of IIT and Indian Institute of Management 2017/18 for a funding research stay of Mr. Bhalerao in the Institute for Sanitary Engineering and Waste Management (ISAH) (personal Ref. ID: 91674911). We would also like to acknowledge the technical support provided by Mr. B. Schwanda, Mrs. K. Kock and Dr. Ing. C. Lorey (ISAH) for the completion of this work.

PY - 2020/5

Y1 - 2020/5

N2 - Polyhydroxyalkanoates (PHAs) present an eco-friendly alternative for conventional plastics. Industrial wastewater from the food industry is a copious source of organic carbon that can be recovered in the form of PHA. However, the wastewater composition varies considerably among the different industries demanding for an industry-specific investigation of the PHA production process. Wastewater from the yeast industry, besides its high concentration in organic carbon, also contains a high ammonium concentration which might decrease the PHA production. Thus, this study aims to investigate PHA production using yeast industry wastewater via an enriched mixed microbial culture (MMC). A less explored cultivation strategy, i.e., continuous cultivation for PHA production was evaluated and compared to the widely used batch cultivation. PHA accumulating MMC was enriched using a sequencing batch reactor (SBR) operated under aerobic dynamic feeding. An MMC dominated by the Thauera species was successfully enriched in the SBR. Experimental results showed that ammonium is indeed required for PHA accumulation and the complete absence of ammonium negatively affects the accumulation process. Using wastewater, batch and continuous feeding strategies, respectively, yielded the PHA accumulation of 72 % and 65 % per dry cell weight. Despite the slightly lower PHA accumulation with continuous cultivation, four times more biomass growth was produced. Consequently, higher theoretical PHA production (270 t/year) can be expected using continuous cultivation in half of the reactor volume (45 m3). Therefore, this study asserts the viability of continuous cultivation as a feasible investigatory tool and PHA production strategy.

AB - Polyhydroxyalkanoates (PHAs) present an eco-friendly alternative for conventional plastics. Industrial wastewater from the food industry is a copious source of organic carbon that can be recovered in the form of PHA. However, the wastewater composition varies considerably among the different industries demanding for an industry-specific investigation of the PHA production process. Wastewater from the yeast industry, besides its high concentration in organic carbon, also contains a high ammonium concentration which might decrease the PHA production. Thus, this study aims to investigate PHA production using yeast industry wastewater via an enriched mixed microbial culture (MMC). A less explored cultivation strategy, i.e., continuous cultivation for PHA production was evaluated and compared to the widely used batch cultivation. PHA accumulating MMC was enriched using a sequencing batch reactor (SBR) operated under aerobic dynamic feeding. An MMC dominated by the Thauera species was successfully enriched in the SBR. Experimental results showed that ammonium is indeed required for PHA accumulation and the complete absence of ammonium negatively affects the accumulation process. Using wastewater, batch and continuous feeding strategies, respectively, yielded the PHA accumulation of 72 % and 65 % per dry cell weight. Despite the slightly lower PHA accumulation with continuous cultivation, four times more biomass growth was produced. Consequently, higher theoretical PHA production (270 t/year) can be expected using continuous cultivation in half of the reactor volume (45 m3). Therefore, this study asserts the viability of continuous cultivation as a feasible investigatory tool and PHA production strategy.

KW - Continuous cultivation

KW - Mixed microbial culture

KW - Polyhydroxyalkanoates

KW - Theoretical polyhydroxyalkanoate production

KW - Yeast industry wastewater

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SP - 595

EP - 602

JO - Journal of Bioscience and Bioengineering

JF - Journal of Bioscience and Bioengineering

SN - 1389-1723

IS - 5

ER -

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