Batch Fermentation of Lignocellulosic Elephant Grass Biomass for 2G Ethanol and Xylitol Production
The solid and growing demand for fuels evidences the necessity of diversifying the countries’ energy matrices. The present work proposed to carry out pretreatment tests, enzymatic hydrolysis, and batch fermentation of elephant grass biomass — a competitive lignocellulosic culture for obtaining ethan...
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Veröffentlicht in: | Bioenergy research 2023-12, Vol.16 (4), p.2219-2228 |
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Format: | Artikel |
Sprache: | eng |
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Zusammenfassung: | The solid and growing demand for fuels evidences the necessity of diversifying the countries’ energy matrices. The present work proposed to carry out pretreatment tests, enzymatic hydrolysis, and batch fermentation of elephant grass biomass — a competitive lignocellulosic culture for obtaining ethanol due to low production costs and high levels of agricultural productivity. As a process and product economy strategy, the production of xylitol integrated with ethanol production was carried out. Therefore, two alkaline pretreatment methodologies were followed by enzymatic hydrolysis to obtain fermentable sugars. The pretreatments proved efficient in making cellulose available and removing the lignin content. The hydrolysates obtained showed 19.9 and 25.6 g/L of total sugars. Then, three fermentation conditions were carried out in each hydrolysate: (i) by the wild yeast strain
Meyerozyma caribbica
CHAP-096, (ii) by the industrial strain
Saccharomyces cerevisiae
PE-02, and (iii) by a combination of both yeasts in a 1:1 (v/v) ratio. A high ethanol yield of 0.42
g
ethanol
/
g
glucose
was reached through the combination of
S. cerevisiae
and
M. caribbica
strains, representing 83% of the maximum theoretical yield (0.511
g
ethanol
/
g
glucose
). The industrial strain
S. cerevisiae
PE-2 was also able to reduce xylose into another important component in biorefinery, xylitol, with a yield of up to 0.61
g
xylitol
/
g
xylose
.
Graphical Abstract |
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ISSN: | 1939-1234 1939-1242 |
DOI: | 10.1007/s12155-022-10559-2 |