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High-Cell-Density Yeast Oil Production with Diluted Substrates Imitating Microalgae Hydrolysate Using a Membrane Bioreactor

Author

Listed:
  • Ayşe Koruyucu

    (Chair of Biochemical Engineering, School of Engineering and Design, Technical University of Munich, 85748 Garching, Germany)

  • Karlis Blums

    (Chair of Biochemical Engineering, School of Engineering and Design, Technical University of Munich, 85748 Garching, Germany)

  • Tillmann Peest

    (Chair of Biochemical Engineering, School of Engineering and Design, Technical University of Munich, 85748 Garching, Germany)

  • Laura Schmack-Rauscher

    (Chair of Biochemical Engineering, School of Engineering and Design, Technical University of Munich, 85748 Garching, Germany)

  • Thomas Brück

    (Werner Siemens-Chair of Synthetic Biotechnology, School of Natural Sciences, Technical University of Munich, 85748 Garching, Germany)

  • Dirk Weuster-Botz

    (Chair of Biochemical Engineering, School of Engineering and Design, Technical University of Munich, 85748 Garching, Germany
    TUM Pilot Plant for Industrial Biotechnology, Technical University of Munich, 85748 Garching, Germany)

Abstract

Microbial oil production from industrial waste streams and biogenic resources, such as biomass hydrolysates, is emerging as a sustainable alternative to use of fossil and vegetable oils. However, the carbon sources of these substrates are typically diluted, leading to low product concentrations and, therefore, high fermentation and downstream processing costs. In this study, high-cell-density yeast oil production with a defined medium, which imitated the sugar composition of a diluted substrate, a typical microalgal biomass hydrolysate, is carried out on a 50 L scale using a membrane bioreactor (MBR) consisting of a microfiltration unit suited for industrial application. The process was run on a semi-continuous mode to reduce operational costs. Oleaginous yeast Cutaneotrichosporon oleaginosus was used as a biocatalyst and lipid production was induced by phosphate deficiency in the medium with a C/P ratio of 3515 g g −1 . In this way, high cellular lipid contents of up to 76.5% ( w/w ) of dry cell mass, an average lipid yield of 32% ( w / w ), and a lipid space–time yield (STY) of up to 8.88 g L −1 d −1 were achieved with final high cell densities of up to 116 g L −1 dry biomass. Furthermore, use of a defined medium and elemental analysis of the yeast cells and yeast oil enabled drawing an accurate carbon mass balance of the production system. Carbon conversion efficiencies—fraction of total carbon supplied in the form of sugars converted into lipids at the end of the process—of up to 61.5% were achieved from diluted substrates using the MBR with total cell retention. Considering these results, it is concluded that utilization of an MBR on a semi-continuous mode would be very reasonable for yeast oil production, enabling high productivities with diluted sugar substrates.

Suggested Citation

  • Ayşe Koruyucu & Karlis Blums & Tillmann Peest & Laura Schmack-Rauscher & Thomas Brück & Dirk Weuster-Botz, 2023. "High-Cell-Density Yeast Oil Production with Diluted Substrates Imitating Microalgae Hydrolysate Using a Membrane Bioreactor," Energies, MDPI, vol. 16(4), pages 1-15, February.
  • Handle: RePEc:gam:jeners:v:16:y:2023:i:4:p:1757-:d:1063824
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    References listed on IDEAS

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    1. Marina Grubišić & Maja Galić Perečinec & Ines Peremin & Katarina Mihajlovski & Sunčica Beluhan & Božidar Šantek & Mirela Ivančić Šantek, 2022. "Optimization of Pretreatment Conditions and Enzymatic Hydrolysis of Corn Cobs for Production of Microbial Lipids by Trichosporon oleaginosus," Energies, MDPI, vol. 15(9), pages 1-16, April.
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