2020
DOI: 10.1007/s00449-020-02344-2
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Redox potential as a key parameter for monitoring and optimization of xylose fermentation with yeast Spathaspora passalidarum under limited-oxygen conditions

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Cited by 29 publications
(14 citation statements)
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“…Biazi et al (2020) worked with a 1.4 L bioreactor and 900 mL of working volume using 30 g/L glucose, 75 g/L xylose, and 20 g/L of initial cell concentration at 30 °C, 48 h, 200 rpm, and a k L a of 8.0 h –1 . On the other hand, Bonan et al (2020) used 27.7 g/L of glucose and 66.3 g/L of xylose in a 3L bioreactor containing 1.4L of working volume, 17.2 g/L of initial cell concentration, at 30 °C, 48 h, 200 rpm, and a k L a of 4.9 h –1 . Both authors were able to obtain ethanol concentrations of 37.0 ± 0.09 g/L and 28.6 ± 0.4 g/L, respectively.…”
Section: Resultsmentioning
confidence: 99%
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“…Biazi et al (2020) worked with a 1.4 L bioreactor and 900 mL of working volume using 30 g/L glucose, 75 g/L xylose, and 20 g/L of initial cell concentration at 30 °C, 48 h, 200 rpm, and a k L a of 8.0 h –1 . On the other hand, Bonan et al (2020) used 27.7 g/L of glucose and 66.3 g/L of xylose in a 3L bioreactor containing 1.4L of working volume, 17.2 g/L of initial cell concentration, at 30 °C, 48 h, 200 rpm, and a k L a of 4.9 h –1 . Both authors were able to obtain ethanol concentrations of 37.0 ± 0.09 g/L and 28.6 ± 0.4 g/L, respectively.…”
Section: Resultsmentioning
confidence: 99%
“…The fermentation times were different in the works, but none of the studies reached high values of Y P/S and Q P . Biazi et al (2020) 58 and Bonan et al (2020) 81 worked with hemicellulosic hydrolysates obtained from acid pretreatment and S. passalidarum. Biazi et al (2020) 58 worked with a 1.4 L bioreactor and 900 mL of working volume using 30 g/L glucose, 75 g/L xylose, and 20 g/L of initial cell concentration at 30 °C, 48 h, 200 rpm, and a k L a of 8.0 h −1 .…”
Section: ■ Results and Discussionmentioning
confidence: 99%
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“… 196 Bonan et al (2020) attained highest ethanol titers of 28.6 g L −1 with 0.31 g g −1 yield and 1.12 g L −1 h −1 productivity with Spathaspora passalidarum at K La (h −1 ) of 45. 54 Hence, an ideal process engineering aspect would be to determine the optimal K La value which maximizes the xylose flux towards the desired product with minimal or no secretion of xylitol, eventually benefiting the cell growth and product formation. Alternative approaches such as overexpression of NOX, modification of the cofactor specificity of XR, or expression of NADH specific XR over NADPH-dependent XR can alleviate the problem of redox imbalance and replenish the flux towards central carbon metabolism.…”
Section: Challenges For Xylose Based Bioproductionmentioning
confidence: 99%
“…Microorganisms that have the Crabtree effect produce ethanol when sugar concentrations are high, even in aerobic conditions. S. passalidarum is a Crabtree negative yeast, and cell production increases with higher aeration, and the choice to produce ethanol or cells depends on the concentration of O2 available to the cells [35,38]. In the case of the SBF with immobilized cells used in this work (shaker), the oxygen transfer was probable impaired due to the bioreactor and support choice, making it difficult to consume xylose and, consequently, to produce ethanol.…”
Section: Sbf With Immobilized and Free S Passalidarum Cellsmentioning
confidence: 99%