Fungal protein and ethanol from lignocelluloses using Rhizopus pellets under simultaneous saccharification, filtration and fermentation (SSFF)

The economic viability of the 2nd generation bioethanol production process cannot rely on a single product but on a biorefinery built around it. In this work, ethanol and fungal biomass (animal feed) were produced from acid-pretreated wheat straw slurry under an innovative simultaneous saccharificat...

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Main Authors: Somayeh FazeliNejad, Jorge A. Ferreira, Tomas Brandberg, Patrik R. Lennartsson, Mohammad J. Taherzadeh
Format: Article
Language:English
Published: Alpha Creation Enterprise 2016-03-01
Series:Biofuel Research Journal
Subjects:
Online Access:http://www.biofueljournal.com/article_12528_45372352f012169e6a847efd412b97be.pdf
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author Somayeh FazeliNejad
Jorge A. Ferreira
Tomas Brandberg
Patrik R. Lennartsson
Mohammad J. Taherzadeh
author_facet Somayeh FazeliNejad
Jorge A. Ferreira
Tomas Brandberg
Patrik R. Lennartsson
Mohammad J. Taherzadeh
author_sort Somayeh FazeliNejad
collection DOAJ
description The economic viability of the 2nd generation bioethanol production process cannot rely on a single product but on a biorefinery built around it. In this work, ethanol and fungal biomass (animal feed) were produced from acid-pretreated wheat straw slurry under an innovative simultaneous saccharification, fermentation, and filtration (SSFF) strategy. A membrane unit separated the solids from the liquid and the latter was converted to biomass or to both biomass and ethanol in the fermentation reactor containing Rhizopus sp. pellets. Biomass yields of up to 0.34 g/g based on the consumed monomeric sugars and acetic acid were achieved. A surplus of glucose in the feed resulted in ethanol production and reduced the biomass yield, whereas limiting glucose concentrations resulted in higher consumption of xylose and acetic acid. The specific growth rate, in the range of 0.013-0.015/h, did not appear to be influenced by the composition of the carbon source. Under anaerobic conditions, an ethanol yield of 0.40 g/g was obtained. The present strategy benefits from the easier separation of the biomass from the medium and the fungus ability to assimilate carbon residuals in comparison with when yeast is used. More specifically, it allows in-situ separation of insoluble solids leading to the production of pure fungal biomass as a value-added product.
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spelling doaj.art-8ce9acab97ab466abe53ca6f1b5f91d82024-03-26T15:13:21ZengAlpha Creation EnterpriseBiofuel Research Journal2292-87822292-87822016-03-013137237810.18331/BRJ2016.3.1.712528Fungal protein and ethanol from lignocelluloses using Rhizopus pellets under simultaneous saccharification, filtration and fermentation (SSFF)Somayeh FazeliNejad0Jorge A. Ferreira1Tomas Brandberg2Patrik R. Lennartsson3Mohammad J. Taherzadeh4Swedish Centre for Resource Recovery, University of Borås, SE 501 90, Borås, SwedenSwedish Centre for Resource Recovery, University of Borås, SE 501 90, Borås, SwedenSwedish Centre for Resource Recovery, University of Borås, SE 501 90, Borås, SwedenSwedish Centre for Resource Recovery, University of Borås, SE 501 90, Borås, SwedenSwedish Centre for Resource Recovery, University of Borås, SE 501 90, Borås, SwedenThe economic viability of the 2nd generation bioethanol production process cannot rely on a single product but on a biorefinery built around it. In this work, ethanol and fungal biomass (animal feed) were produced from acid-pretreated wheat straw slurry under an innovative simultaneous saccharification, fermentation, and filtration (SSFF) strategy. A membrane unit separated the solids from the liquid and the latter was converted to biomass or to both biomass and ethanol in the fermentation reactor containing Rhizopus sp. pellets. Biomass yields of up to 0.34 g/g based on the consumed monomeric sugars and acetic acid were achieved. A surplus of glucose in the feed resulted in ethanol production and reduced the biomass yield, whereas limiting glucose concentrations resulted in higher consumption of xylose and acetic acid. The specific growth rate, in the range of 0.013-0.015/h, did not appear to be influenced by the composition of the carbon source. Under anaerobic conditions, an ethanol yield of 0.40 g/g was obtained. The present strategy benefits from the easier separation of the biomass from the medium and the fungus ability to assimilate carbon residuals in comparison with when yeast is used. More specifically, it allows in-situ separation of insoluble solids leading to the production of pure fungal biomass as a value-added product.http://www.biofueljournal.com/article_12528_45372352f012169e6a847efd412b97be.pdfCellulosic ethanolAnimal feedRhizopus spSSFFWheat Straw
spellingShingle Somayeh FazeliNejad
Jorge A. Ferreira
Tomas Brandberg
Patrik R. Lennartsson
Mohammad J. Taherzadeh
Fungal protein and ethanol from lignocelluloses using Rhizopus pellets under simultaneous saccharification, filtration and fermentation (SSFF)
Biofuel Research Journal
Cellulosic ethanol
Animal feed
Rhizopus sp
SSFF
Wheat Straw
title Fungal protein and ethanol from lignocelluloses using Rhizopus pellets under simultaneous saccharification, filtration and fermentation (SSFF)
title_full Fungal protein and ethanol from lignocelluloses using Rhizopus pellets under simultaneous saccharification, filtration and fermentation (SSFF)
title_fullStr Fungal protein and ethanol from lignocelluloses using Rhizopus pellets under simultaneous saccharification, filtration and fermentation (SSFF)
title_full_unstemmed Fungal protein and ethanol from lignocelluloses using Rhizopus pellets under simultaneous saccharification, filtration and fermentation (SSFF)
title_short Fungal protein and ethanol from lignocelluloses using Rhizopus pellets under simultaneous saccharification, filtration and fermentation (SSFF)
title_sort fungal protein and ethanol from lignocelluloses using rhizopus pellets under simultaneous saccharification filtration and fermentation ssff
topic Cellulosic ethanol
Animal feed
Rhizopus sp
SSFF
Wheat Straw
url http://www.biofueljournal.com/article_12528_45372352f012169e6a847efd412b97be.pdf
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