4.6 Article

Effective application of immobilized second generation industrial Saccharomyces cerevisiae strain on consolidated bioprocessing

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NEW BIOTECHNOLOGY
卷 78, 期 -, 页码 153-161

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ELSEVIER
DOI: 10.1016/j.nbt.2023.10.011

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Consolidated bioprocessing; Recombinant Saccharomyces cerevisiae; Immobilized cells; Enzyme production

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This study successfully applied immobilized yeast cells in integrated bioprocessing, enabling enzyme access to substrate polymers. The optimal cell load for consolidated bioprocessing (CBP) was selected, and diffusional effects were observed with immobilized cells under static conditions. However, agitation mitigated mass transfer limitations and achieved the same substrate consumption rate as free cells. Immobilized cells achieved 100% hydrolysis and consumption of all substrates offered within 12 hours. This is the first report of successful application of immobilized yeast cells in CBP processes, a promising technology for bioethanol production.
Integrated bioprocessing strategies can facilitate ethanol production from both cellulose and hemicellulose fractions of lignocellulosic biomass. Consolidated bioprocessing (CBP) is an approach that combines enzyme production, biomass hydrolysis and sugar fermentation in a single step. However, technologies that propose the use of microorganisms together with solid biomass present the difficulty of the recovery and reuse of the biocatalyst, which can be overcome by cell immobilization. In this regard, this work applied immobilized cells of AC14 yeast, a recombinant yeast that secretes 7 hydrolytic enzymes, in the CBP process in a successful proof-of concept for the enzyme access to the substrate polymers. The most appropriate cell load for CBP under the conditions studied with immobilized cells was selected among three optical densities (OD) 10, 55 and 100. These experiments were performed with free cells to ensure that the results were not biased by mass limitations effects. OD 10 achieved 100% of the sugar consumption and the higher specific production of enzymes, being selected for further studies. Diffusional effects were observed with immobilized cells under static conditions. However, mass transfer limitations were mitigated under agitation, with an 18.5% increase in substrate consumption rate (from 2.7 to 3.5 g/L/h), reaching the same substrate uptake rates as free cells. In addition, immobilized cells achieved 100% hydrolysis and consumption of all substrates offered within only 12 h. Overall, this is the first report of a successful application of immobilized yeast cells in CBP processes for bioethanol production, a promising technology that can be extended to other biorefinery bioproducts.

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