Literature DB >> 22133438

An innovative biocatalyst for production of ethanol from xylose in a continuous bioreactor.

C R Silva1, T C Zangirolami, J P Rodrigues, K Matugi, R C Giordano, R L C Giordano.   

Abstract

The use of the hemicellulose fraction of biomass may be important for the feasibility of the production of second generation bioethanol. Wild strains of Saccharomyces cerevisiae are widely used in industry for production of 1st generation ethanol, and the robustness of this yeast is an important advantage in large scale applications. Isomerization of xylose to xylulose is an essential step in this process. This reaction is catalyzed by glucose isomerase (GI). A new biocatalyst is presented here for the simultaneous isomerization and fermentation (SIF) of xylose. GI from Streptomyces rubiginosus was immobilized in chitosan, through crosslinking with glutaraldehyde, and the support containing the immobilized GI (IGI-Ch) was co-immobilized with S. cerevisiae, in calcium alginate gel. The immobilization experiments led to high immobilized protein loads (30-68 mg × g(support)(-1)), high yields (circa of 100%) and high recovered enzyme activity (>90%). The IGI-Ch derivative with maximum activity presented 1700 IU × g(catalyst)(-1), almost twice the activity of a commercial immobilized GI, GENSWEET(®) IGI-HF. At typical operational conditions for xylose SIF operation (pH 5, 30-35 °C, presence of nutrients and ethanol concentrations in the medium up to 70 L(-1)), both derivatives, IGI-Ch and GENSWEET(®) IGI-HF retained app. 90% of the initial activity after 120 h, while soluble GI was almost completely inactive at pH 5, 30 °C. The isomerization xylose/xylulose, catalyzed by IGI-Ch, reached the equilibrium in batch experiments after 4h, with 12,000 IU × L(-1) (7 g(der) × L(-1)), at pH 5 and 30 °C, in the presence of fermentation nutrients. After co-immobilization of IGI-Ch with yeast in alginate gel, this biocatalyst succeeded in producing 12 g × L(-1) of ethanol, 9.5 g × L(-1) of xylitol, 2.5 g × L(-1) of glycerol and 1.9 g × L(-1) of acetate after consumption of 50 g × L(-1) of xylose, in 48 h, using 32.5 × 10(3) IU × L(-1) and 20 g(yeast) × L(-1), at 35 °C and initial pH 5.3.
Copyright © 2011 Elsevier Inc. All rights reserved.

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Year:  2011        PMID: 22133438     DOI: 10.1016/j.enzmictec.2011.09.005

Source DB:  PubMed          Journal:  Enzyme Microb Technol        ISSN: 0141-0229            Impact factor:   3.493


  4 in total

1.  Cell Immobilization Using Alginate-Based Beads as a Protective Technique against Stressful Conditions of Hydrolysates for 2G Ethanol Production.

Authors:  Raiane C Soares; Teresa C Zangirolami; Raquel L C Giordano; Mekonnen M Demeke; Johan M Thevelein; Thais S Milessi
Journal:  Polymers (Basel)       Date:  2022-06-14       Impact factor: 4.967

2.  Metabolic fluxes-oriented control of bioreactors: a novel approach to tune micro-aeration and substrate feeding in fermentations.

Authors:  Thiago José Barbosa Mesquita; Cíntia Regina Sargo; José Roberto Fuzer; Sheyla Alexandra Hidalgo Paredes; Roberto de Campos Giordano; Antonio Carlos Luperni Horta; Teresa Cristina Zangirolami
Journal:  Microb Cell Fact       Date:  2019-09-04       Impact factor: 5.328

3.  Repeated batches as a strategy for high 2G ethanol production from undetoxified hemicellulose hydrolysate using immobilized cells of recombinant Saccharomyces cerevisiae in a fixed-bed reactor.

Authors:  Thais S Milessi; Caroline L Perez; Teresa C Zangirolami; Felipe A S Corradini; Juliana P Sandri; Maria R Foulquié-Moreno; Roberto C Giordano; Johan M Thevelein; Raquel L C Giordano
Journal:  Biotechnol Biofuels       Date:  2020-05-11       Impact factor: 6.040

4.  Bioelectricity versus bioethanol from sugarcane bagasse: is it worth being flexible?

Authors:  Felipe F Furlan; Renato Tonon Filho; Fabio Hpb Pinto; Caliane Bb Costa; Antonio Jg Cruz; Raquel Lc Giordano; Roberto C Giordano
Journal:  Biotechnol Biofuels       Date:  2013-10-03       Impact factor: 6.040

  4 in total

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