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Biobutanol production from coffee silverskin

BACKGROUND: Coffee silverskin, a by-product from coffee roasting industries, was evaluated as a feedstock for biobutanol production by acetone–butanol–ethanol fermentation. This lignocellulosic biomass contained approximately 30% total carbohydrates and 30% lignin. Coffee silverskin was subjected to...

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Autores principales: Hijosa-Valsero, María, Garita-Cambronero, Jerson, Paniagua-García, Ana I., Díez-Antolínez, Rebeca
Formato: Online Artículo Texto
Lenguaje:English
Publicado: BioMed Central 2018
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6158808/
https://www.ncbi.nlm.nih.gov/pubmed/30261894
http://dx.doi.org/10.1186/s12934-018-1002-z
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author Hijosa-Valsero, María
Garita-Cambronero, Jerson
Paniagua-García, Ana I.
Díez-Antolínez, Rebeca
author_facet Hijosa-Valsero, María
Garita-Cambronero, Jerson
Paniagua-García, Ana I.
Díez-Antolínez, Rebeca
author_sort Hijosa-Valsero, María
collection PubMed
description BACKGROUND: Coffee silverskin, a by-product from coffee roasting industries, was evaluated as a feedstock for biobutanol production by acetone–butanol–ethanol fermentation. This lignocellulosic biomass contained approximately 30% total carbohydrates and 30% lignin. Coffee silverskin was subjected to autohydrolysis at 170 °C during 20 min, with a biomass-to-solvent ratio of 20%, and a subsequent enzymatic hydrolysis with commercial enzymes in order to release simple sugars. The fermentability of the hydrolysate was assessed with four solventogenic strains from the genus Clostridium. In addition, fermentation conditions were optimised via response surface methodology to improve butanol concentration in the final broth. RESULTS: The coffee silverskin hydrolysate contained 34.39 ± 2.61 g/L total sugars, which represents a sugar recovery of 34 ± 3%. It was verified that this hydrolysate was fermentable without the need of any detoxification method and that C. beijerinckii CECT 508 was the most efficient strain for butanol production, attaining final values of 4.14 ± 0.21 g/L acetone, 7.02 ± 0.27 g/L butanol and 0.25 ± 0.01 g/L ethanol, consuming 76.5 ± 0.8% sugars and reaching a butanol yield of 0.269 ± 0.008 g(B)/g(S) under optimal conditions. CONCLUSIONS: Coffee silverskin could be an adequate feedstock for butanol production in biorefineries. When working with complex matrices like lignocellulosic biomass, it is essential to select an adequate bacterial strain and to optimize its fermentation conditions (such as pH, temperature or CaCO(3) concentration). [Image: see text] ELECTRONIC SUPPLEMENTARY MATERIAL: The online version of this article (10.1186/s12934-018-1002-z) contains supplementary material, which is available to authorized users.
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spelling pubmed-61588082018-10-01 Biobutanol production from coffee silverskin Hijosa-Valsero, María Garita-Cambronero, Jerson Paniagua-García, Ana I. Díez-Antolínez, Rebeca Microb Cell Fact Research BACKGROUND: Coffee silverskin, a by-product from coffee roasting industries, was evaluated as a feedstock for biobutanol production by acetone–butanol–ethanol fermentation. This lignocellulosic biomass contained approximately 30% total carbohydrates and 30% lignin. Coffee silverskin was subjected to autohydrolysis at 170 °C during 20 min, with a biomass-to-solvent ratio of 20%, and a subsequent enzymatic hydrolysis with commercial enzymes in order to release simple sugars. The fermentability of the hydrolysate was assessed with four solventogenic strains from the genus Clostridium. In addition, fermentation conditions were optimised via response surface methodology to improve butanol concentration in the final broth. RESULTS: The coffee silverskin hydrolysate contained 34.39 ± 2.61 g/L total sugars, which represents a sugar recovery of 34 ± 3%. It was verified that this hydrolysate was fermentable without the need of any detoxification method and that C. beijerinckii CECT 508 was the most efficient strain for butanol production, attaining final values of 4.14 ± 0.21 g/L acetone, 7.02 ± 0.27 g/L butanol and 0.25 ± 0.01 g/L ethanol, consuming 76.5 ± 0.8% sugars and reaching a butanol yield of 0.269 ± 0.008 g(B)/g(S) under optimal conditions. CONCLUSIONS: Coffee silverskin could be an adequate feedstock for butanol production in biorefineries. When working with complex matrices like lignocellulosic biomass, it is essential to select an adequate bacterial strain and to optimize its fermentation conditions (such as pH, temperature or CaCO(3) concentration). [Image: see text] ELECTRONIC SUPPLEMENTARY MATERIAL: The online version of this article (10.1186/s12934-018-1002-z) contains supplementary material, which is available to authorized users. BioMed Central 2018-09-27 /pmc/articles/PMC6158808/ /pubmed/30261894 http://dx.doi.org/10.1186/s12934-018-1002-z Text en © The Author(s) 2018 Open AccessThis article is distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution, and reproduction in any medium, provided you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made. The Creative Commons Public Domain Dedication waiver (http://creativecommons.org/publicdomain/zero/1.0/) applies to the data made available in this article, unless otherwise stated.
spellingShingle Research
Hijosa-Valsero, María
Garita-Cambronero, Jerson
Paniagua-García, Ana I.
Díez-Antolínez, Rebeca
Biobutanol production from coffee silverskin
title Biobutanol production from coffee silverskin
title_full Biobutanol production from coffee silverskin
title_fullStr Biobutanol production from coffee silverskin
title_full_unstemmed Biobutanol production from coffee silverskin
title_short Biobutanol production from coffee silverskin
title_sort biobutanol production from coffee silverskin
topic Research
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6158808/
https://www.ncbi.nlm.nih.gov/pubmed/30261894
http://dx.doi.org/10.1186/s12934-018-1002-z
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