Abstract
We investigated the fermentation of a mixture of oat and soybean hulls (1:1) subjected to acid (AH) or enzymatic (EH) hydrolyses, with both showing high osmotic pressures (> 1200 Osm kg−1) for the production of ethanol. Yeasts of genera Spathaspora, Scheffersomyces, Sugiymaella, and Candida, most of them biodiverse Brazilian isolates and previously untested in bioprocesses, were cultivated in these hydrolysates. Spathaspora passalidarum UFMG-CM-469 showed the best ethanol production kinetics in suspended cells cultures in acid hydrolysate, under microaerobic and anaerobic conditions. This strain was immobilized in LentiKats® (polyvinyl alcohol) and cultured in AH and EH. Supplementation of hydrolysates with crude yeast extract and peptone was also performed. The highest ethanol production was obtained using hydrolysates supplemented with crude yeast extract (AH-CYE and EH-CYE) showing yields of 0.40 and 0.44 g g−1, and productivities of 0.39 and 0.29 g (L h)−1, respectively. The reuse of the immobilized cells was tested in sequential fermentations of AH-CYE, EH-CYE, and a mixture of acid and enzymatic hydrolysates (AEH-CYE) operated under batch fluidized bed, with ethanol yields ranging from 0.31 to 0.40 g g−1 and productivities from 0.14 to 0.23 g (L h)−1. These results warrant further research using Spathaspora yeasts for second-generation ethanol production.
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Acknowledgements
The authors wish to thank Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq), Coordenação do Aperfeiçoamento de Pessoal do Ensino Superior (CAPES), Finance Code 001, and FAPERGS for their financial support and scholarships for this project. The authors thank Cereais Naturale (Lagoa Vermelha, RS, Brazil) for supplying the oat hulls.
Supplementary Information
Supplementary Material 2. Performance of yeasts fermenting concentrated hydrolysate resulting from acid treatment (AH) in an orbital shaker at 28 oC and 180 rpm under microaerophilic conditions.
Figure S2.1. Fermentation of concentrated hydrolysate resulting from acid treatment (AH) in orbital shaker at 28 °C and 180 rpm by Spathaspora brasiliensis UFMG-HMD-19.3. (A) Biomass formation (CFU mL−1). (B) Kinetics of substrates consumption and products formation; (open circle) Glucose, (open square) Xylose, (filled circle) Ethanol, (filled square) Xylitol, and (filled triangle) glycerol. Results are the mean of duplicates.
Figure S2.2. Fermentation of concentrated hydrolysate resulting from acid treatment (AH) in orbital shaker at 28 °C and 180 rpm by Spathaspora girioi UFMG-CM-Y302. (A) Biomass formation (CFU mL−1). (B) Kinetics of substrates consumption and products formation; (open circle) Glucose, (open square) Xylose, (filled circle) Ethanol, (filled square) Xylitol, and (filled triangle) glycerol. Results are the mean of duplicates.
Figure 2.3. Fermentation of concentrated hydrolysate resulting from acid treatment (AH) in orbital shaker at 28 °C and 180 rpm by Spathaspora roraimanensis UFMG-XMD-23.2. (A) Biomass formation (CFU mL−1). (B) Kinetics of substrates consumption and products formation; (open circle) Glucose, (open square) Xylose, (filled circle) Ethanol, (filled square) Xylitol, and (filled triangle) glycerol. Results are the mean of duplicates.
Figure S2.4. Fermentation of concentrated hydrolysate resulting from acid treatment (AH) in orbital shaker at 28 °C and 180 rpm by Spathaspora xylofermentans UFMG-HMD-23.3. (A) Biomass formation (CFU mL−1). (B) Kinetics of substrates consumption and products formation; (open circle) Glucose, (open square) Xylose, (filled circle) Ethanol, (filled square) Xylitol, and (filled triangle) glycerol. Results are the mean of duplicates.
Figure S2.5. Fermentation of concentrated hydrolysate resulting from acid treatment (AH) in orbital shaker at 28 °C and 180 rpm by Spathaspora passalidarum CBS-10501. (A) Biomass formation (CFU mL−1). (B) Kinetics of substrates consumption and products formation; (open circle) Glucose, (open square) Xylose, (filled circle) Ethanol, (filled square) Xylitol, and (filled triangle) glycerol. Results are the mean of duplicates.
Figure S2.6. Fermentation of concentrated hydrolysate resulting from acid treatment (AH) in orbital shaker at 28 °C and 180 rpm by Spathaspora passalidarum UFMG-CM-469. (A) Biomass formation (CFU mL−1). (B) Kinetics of substrates consumption and products formation; (open circle) Glucose, (open square) Xylose, (filled circle) Ethanol, (filled square) Xylitol, and (filled triangle) glycerol. Results are the mean of duplicates.
Figure S2.7. Fermentation of concentrated hydrolysate resulting from acid treatment (AH) in orbital shaker at 28 °C and 180 rpm by Candida guilliermondii NRRL Y-2075. (A) Biomass formation (CFU mL−1). (B) Kinetics of substrates consumption and products formation; (open circle) Glucose, (open square) Xylose, (filled circle) Ethanol, (filled square) Xylitol, and (filled triangle) glycerol. Results are the mean of duplicates.
Figure S2.8. Fermentation of concentrated hydrolysate resulting from acid treatment (AH) in orbital shaker at 28 °C and 180 rpm by Scheffersomyces queiroziae UFMG-CM-416. (A) Biomass formation (CFU mL−1). (B) Kinetics of substrates consumption and products formation; (open circle) Glucose, (open square) Xylose, (filled circle) Ethanol, (filled square) Xylitol, and (filled triangle) glycerol. Results are the mean of duplicates.
Figure S2.9. Fermentation of concentrated hydrolysate resulting from acid treatment (AH) in orbital shaker at 28 °C and 180 rpm by Scheffersomyces amazonensis UFMG-CM-418. (A) Biomass formation (CFU mL−1). (B) Kinetics of substrates consumption and products formation; (open circle) Glucose, (open square) Xylose, (filled circle) Ethanol, (filled square) Xylitol, and (filled triangle) glycerol. Results are the mean of duplicates.
Figure S2.10. Fermentation of concentrated hydrolysate resulting from acid treatment (AH) in orbital shaker at 28 °C and 180 rpm by Sugiymaella xylanicola UFMG-CM-Y1884. (A) Biomass formation (CFU mL−1). (B) Kinetics of substrates consumption and products formation; (open circle) Glucose, (open square) Xylose, (filled circle) Ethanol, (filled square) Xylitol, and (filled triangle) glycerol. Results are the mean of duplicates.
Figure S2.11. Fermentation of concentrated hydrolysate resulting from acid treatment (AH) in orbital shaker at 28 °C and 180 rpm by Scheffersomyces stipitis UFMG-IMH- 43.2. (A) Biomass formation (CFU mL−1). (B) Kinetics of substrates consumption and products formation; (open circle) Glucose, (open square) Xylose, (filled circle) Ethanol, (filled square) Xylitol, and (filled triangle) glycerol. Results are the mean of duplicates.
Figure S2.12. Fermentation of concentrated hydrolysate resulting from acid treatment (AH) in orbital shaker at 28 °C and 180 rpm by Saccharomyces cerevisiae YRH1415. (A) Biomass formation (CFU mL−1). (B) Kinetics of substrates consumption and products formation; (open circle) Glucose, (open square) Xylose, (filled circle) Ethanol, (filled square) Xylitol, and (filled triangle) glycerol. Results are the mean of duplicates.
Supplementary Material 3. Fermentation of AH and EH by Sp. passalidarum UFMG-CM-469 with immobilized cells in LentiKats® and the effect of supplementation.
Figure S3.1. Kinetics of substrate consumption and products formation in fermentation of AH (A), AH-CYE (B), and AH-CYEP (C) by Sp. passalidarum UFMG-CM-469 immobilized in LentiKats® in orbital shaker at 28 °C and 180 rpm. (open circle) Glucose, (open square) Xylose, (filled circle) Ethanol, (filled square) Xylitol, and (filled triangle) glycerol. Results are the mean of duplicates.
Figure S3.2. Kinetics of substrate consumption and products formation in fermentation of EH (A), EH-CYE (B), and EH-CYEP (C) by Sp. passalidarum UFMG-CM-469 immobilized in LentiKats® in orbital shaker at 28 °C and 180 rpm. (open circle) Glucose, (open square) Xylose, (filled circle) Ethanol, (filled square) Xylitol, and (filled triangle) glycerol. Results are the mean of duplicates.
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Cortivo, P.R.D., Aydos, L.F., Hickert, L.R. et al. Performance of xylose-fermenting yeasts in oat and soybean hulls hydrolysate and improvement of ethanol production using immobilized cell systems. Biotechnol Lett 43, 2011–2026 (2021). https://doi.org/10.1007/s10529-021-03182-2
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DOI: https://doi.org/10.1007/s10529-021-03182-2