Literature DB >> 23454083

Bioethanol production from mixed sugars by Scheffersomyces stipitis free and immobilized cells, and co-cultures with Saccharomyces cerevisiae.

Isabella De Bari1, Paola De Canio, Daniela Cuna, Federico Liuzzi, Angela Capece, Patrizia Romano.   

Abstract

Bioethanol can be produced from several biomasses including lignocellulosic materials. Besides 6-carbon sugars that represent the prevalent carbohydrates, some of these feedstocks contain significant amounts of 5-carbon sugars. One common limit of the major part of the xylose-fermenting yeasts is the diauxic shift between the uptake of glucose and xylose during the fermentation of mixed syrups. Thus, optimized fermentation strategies are required. In this paper the ability of Scheffersomyces stipitis strain NRRLY-11544 to ferment mixed syrups with a total sugar concentration in the range 40-80 g/L was investigated by using mono cultures, co-cultures with Saccharomyces cerevisiae strain Bakers Yeast Type II and single cultures immobilized in silica-hydrogel films. The experimental design for the fermentations with immobilized cells included the process analysis in function of two parameters: the fraction of the gel in the broth and the concentration of the cells loaded in the gel. Furthermore, for each total sugars level, the fermentative course of S. stipitis was analyzed at several glucose-to xylose ratios. The results indicated that the use of S. stipitis and S. cerevisiae in free co-cultures ensured faster processes than single cultures of S. stipitis either free or immobilized. However, the rapid production of ethanol by S. cerevisiae inhibited S. stipitis and caused a stuck of the process. Immobilization of S. stipitis in silica-hydrogel increased the relative consumption rate of xylose-to-glucose by 2-6 times depending on the composition of the fermentation medium. Furthermore the films performances appeared stable over three weeks of continuous operations. However, on the whole, the final process yields obtained with the immobilized cells were not meaningfully different from that of the free cells. This was probably due to concurrent fermentations operated by the cells released in the broth. Optimization of the carrier characteristics could improve the performances of the process with immobilized cells.
Copyright © 2013 Elsevier B.V. All rights reserved.

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Year:  2013        PMID: 23454083     DOI: 10.1016/j.nbt.2013.02.003

Source DB:  PubMed          Journal:  N Biotechnol        ISSN: 1871-6784            Impact factor:   5.079


  5 in total

1.  Identification of strain isolated from dates (Phœnix dactylifera L.) for enhancing very high gravity ethanol production.

Authors:  Hayet Djelal; Sofien Chniti; Monia Jemni; Amélie Weill; Walaa Sayed; Abdeltif Amrane
Journal:  Environ Sci Pollut Res Int       Date:  2016-11-12       Impact factor: 4.223

2.  Influence of operational parameters on the fluid-side mass transfer resistance observed in a packed bed bioreactor.

Authors:  Amir Hussain; Martin Kangwa; Ahmed Gad Abo-Elwafa; Marcelo Fernandez-Lahore
Journal:  AMB Express       Date:  2015-05-01       Impact factor: 3.298

3.  Operational parameters and their influence on particle-side mass transfer resistance in a packed bed bioreactor.

Authors:  Amir Hussain; Martin Kangwa; Nivedita Yumnam; Marcelo Fernandez-Lahore
Journal:  AMB Express       Date:  2015-08-14       Impact factor: 3.298

4.  Notable mixed substrate fermentation by native Kodamaea ohmeri strains isolated from Lagenaria siceraria flowers and ethanol production on paddy straw hydrolysates.

Authors:  Shalley Sharma; Anju Arora; Pankhuri Sharma; Surender Singh; Lata Nain; Debarati Paul
Journal:  Chem Cent J       Date:  2018-02-05       Impact factor: 4.215

5.  Encapsulation enhances protoplast fusant stability.

Authors:  Jordan Gulli; Eugene Kroll; Frank Rosenzweig
Journal:  Biotechnol Bioeng       Date:  2020-03-25       Impact factor: 4.530

  5 in total

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