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Strategies to achieve high productivity, high conversion, and high yield in yeast fermentation of algal biomass hydrolysate
The conversion of carbohydrates in biomass via fermentation is an important component of an overall strategy to decarbonize the production of fuels and chemicals. Owing to the cost and resources required to produce biomass hydrolysates, the economic and environmental sustainability of these fermenta...
Autores principales: | , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
John Wiley and Sons Inc.
2021
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8961051/ https://www.ncbi.nlm.nih.gov/pubmed/35382533 http://dx.doi.org/10.1002/elsc.202100095 |
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author | Huang, Xing‐Feng Reardon, Kenneth F. |
author_facet | Huang, Xing‐Feng Reardon, Kenneth F. |
author_sort | Huang, Xing‐Feng |
collection | PubMed |
description | The conversion of carbohydrates in biomass via fermentation is an important component of an overall strategy to decarbonize the production of fuels and chemicals. Owing to the cost and resources required to produce biomass hydrolysates, the economic and environmental sustainability of these fermentation processes requires that they operate with high yields, sugar conversion, and productivity. Immobilized‐cell technology in a continuous bioprocess can achieve significantly higher volumetric productivities than is possible from standard batch fermentation using free cells. Here, we demonstrate approaches for improvement of ethanol yield from algal hydrolysates and a mock hydrolysate medium. Saccharomyces cerevisiae was immobilized in alginate and incorporated into a two‐column immobilized cell reactor system. Furthermore, the yeast quorum‐sensing molecule, 2‐phenylethanol, was added to improve ethanol yield by restricting growth and diverting sugar to ethanol. The bioreactor system could achieve high ethanol volumetric productivity (>20 g/L(reactor)·h) and high glucose conversion (>99%) in mock hydrolysate, while the addition of 0.2% 2‐phenylethanol resulted in 4.9% higher ethanol yield. With an algal hydrolysate of <10 g/L sugar, the ethanol volumetric productivity reached 9.8 g/L(reactor)·h, and the addition of 0.2% 2‐phenylethanol increased the ethanol yield by up to 7.4%. These results demonstrate the feasibility of novel strategies to achieve sustainability goals in biomass conversions. |
format | Online Article Text |
id | pubmed-8961051 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2021 |
publisher | John Wiley and Sons Inc. |
record_format | MEDLINE/PubMed |
spelling | pubmed-89610512022-04-04 Strategies to achieve high productivity, high conversion, and high yield in yeast fermentation of algal biomass hydrolysate Huang, Xing‐Feng Reardon, Kenneth F. Eng Life Sci Research Articles The conversion of carbohydrates in biomass via fermentation is an important component of an overall strategy to decarbonize the production of fuels and chemicals. Owing to the cost and resources required to produce biomass hydrolysates, the economic and environmental sustainability of these fermentation processes requires that they operate with high yields, sugar conversion, and productivity. Immobilized‐cell technology in a continuous bioprocess can achieve significantly higher volumetric productivities than is possible from standard batch fermentation using free cells. Here, we demonstrate approaches for improvement of ethanol yield from algal hydrolysates and a mock hydrolysate medium. Saccharomyces cerevisiae was immobilized in alginate and incorporated into a two‐column immobilized cell reactor system. Furthermore, the yeast quorum‐sensing molecule, 2‐phenylethanol, was added to improve ethanol yield by restricting growth and diverting sugar to ethanol. The bioreactor system could achieve high ethanol volumetric productivity (>20 g/L(reactor)·h) and high glucose conversion (>99%) in mock hydrolysate, while the addition of 0.2% 2‐phenylethanol resulted in 4.9% higher ethanol yield. With an algal hydrolysate of <10 g/L sugar, the ethanol volumetric productivity reached 9.8 g/L(reactor)·h, and the addition of 0.2% 2‐phenylethanol increased the ethanol yield by up to 7.4%. These results demonstrate the feasibility of novel strategies to achieve sustainability goals in biomass conversions. John Wiley and Sons Inc. 2021-11-10 /pmc/articles/PMC8961051/ /pubmed/35382533 http://dx.doi.org/10.1002/elsc.202100095 Text en © 2021 The Authors. Engineering in Life Sciences published by Wiley‐VCH GmbH https://creativecommons.org/licenses/by-nc-nd/4.0/This is an open access article under the terms of the http://creativecommons.org/licenses/by-nc-nd/4.0/ (https://creativecommons.org/licenses/by-nc-nd/4.0/) License, which permits use and distribution in any medium, provided the original work is properly cited, the use is non‐commercial and no modifications or adaptations are made. |
spellingShingle | Research Articles Huang, Xing‐Feng Reardon, Kenneth F. Strategies to achieve high productivity, high conversion, and high yield in yeast fermentation of algal biomass hydrolysate |
title | Strategies to achieve high productivity, high conversion, and high yield in yeast fermentation of algal biomass hydrolysate |
title_full | Strategies to achieve high productivity, high conversion, and high yield in yeast fermentation of algal biomass hydrolysate |
title_fullStr | Strategies to achieve high productivity, high conversion, and high yield in yeast fermentation of algal biomass hydrolysate |
title_full_unstemmed | Strategies to achieve high productivity, high conversion, and high yield in yeast fermentation of algal biomass hydrolysate |
title_short | Strategies to achieve high productivity, high conversion, and high yield in yeast fermentation of algal biomass hydrolysate |
title_sort | strategies to achieve high productivity, high conversion, and high yield in yeast fermentation of algal biomass hydrolysate |
topic | Research Articles |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8961051/ https://www.ncbi.nlm.nih.gov/pubmed/35382533 http://dx.doi.org/10.1002/elsc.202100095 |
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