First‐ and second‐generation integrated process for bioethanol production: Fermentation of molasses diluted with hemicellulose hydrolysate by recombinant Saccharomyces cerevisiae

Author:

de Oliveira Pereira Isabela1,dos Santos Ângela A.2,Guimarães Nick C.1,Lima Cleilton S.3,Zanella Eduardo2,Matsushika Akinori45,Rabelo Sarita C.6,Stambuk Boris U.2,Ienczak Jaciane L.1ORCID

Affiliation:

1. Department of Chemical Engineering and Food Engineering (EQA) Universidade Federal de Santa Catarina Florianópolis Brazil

2. Department of Biochemistry Federal University of Santa Catarina Florianópolis Brazil

3. Department of Biotechnology Engineering College of Lorena University of São Paulo (USP) Lorena Brazil

4. Research Institute for Sustainable Chemistry, National Institute of Advanced Industrial Science and Technology Higashi‐Hiroshima Japan

5. Graduate School of Integrated Sciences for Life Hiroshima University Higashi‐Hiroshima Japan

6. Department of Bioprocess and Biotechnology College of Agriculture Sciences São Paulo State University (UNESP) Botucatu Brazil

Abstract

AbstractThe integration of first‐ (1G) and second‐generation (2G) ethanol production by adding sugarcane juice or molasses to lignocellulosic hydrolysates offers the possibility to overcome the problem of inhibitors (acetic acid, furfural, hydroxymethylfurfural and phenolic compounds), and add nutrients (such as salts, sugars and nitrogen sources) to the fermentation medium, allowing the production of higher ethanol titers. In this work, an 1G2G production process was developed with hemicellulosic hydrolysate (HH) from a diluted sulfuric acid pretreatment of sugarcane bagasse and sugarcane molasses. The industrial Saccharomyces cerevisiae CAT‐1 was genetically modified for xylose consumption and used for co‐fermentation of sucrose, fructose, glucose, and xylose. The fed‐batch fermentation with high cell density that mimics an industrial fermentation was performed at bench scale fermenter, achieved high volumetric ethanol productivity of 1.59 g L−1 h−1, 0.39 g g−1 of ethanol yield, and 44.5 g L−1 ethanol titer, and shown that the yeast was able to consume all the sugars present in must simultaneously. With the results, it was possible to establish a mass balance for the global process: from pretreatment to the co‐fermentation of molasses and HH, and it was possible to establish an effective integrated process (1G2G) with sugarcane molasses and HH co‐fermentation employing a recombinant yeast.

Publisher

Wiley

Subject

Applied Microbiology and Biotechnology,Bioengineering,Biotechnology

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