Biobutanol production from coffee silverskin

Abstract 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 subj...

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Main Authors: María Hijosa-Valsero, Jerson Garita-Cambronero, Ana I. Paniagua-García, Rebeca Díez-Antolínez
Format: Article
Language:English
Published: BMC 2018-09-01
Series:Microbial Cell Factories
Subjects:
Online Access:http://link.springer.com/article/10.1186/s12934-018-1002-z
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spelling doaj-bbca5b8d0d2242958a54a4220a17e5c22020-11-25T00:50:45ZengBMCMicrobial Cell Factories1475-28592018-09-011711910.1186/s12934-018-1002-zBiobutanol production from coffee silverskinMaría Hijosa-Valsero0Jerson Garita-Cambronero1Ana I. Paniagua-García2Rebeca Díez-Antolínez3Centro de Biocombustibles y Bioproductos, Instituto Tecnológico Agrario de Castilla y León (ITACyL)Centro de Biocombustibles y Bioproductos, Instituto Tecnológico Agrario de Castilla y León (ITACyL)Centro de Biocombustibles y Bioproductos, Instituto Tecnológico Agrario de Castilla y León (ITACyL)Centro de Biocombustibles y Bioproductos, Instituto Tecnológico Agrario de Castilla y León (ITACyL)Abstract 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 gB/gS 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 CaCO3 concentration).http://link.springer.com/article/10.1186/s12934-018-1002-zCoffee silverskinLignocellulosic wastesPretreatmentButanolABE fermentationBiorefinery
collection DOAJ
language English
format Article
sources DOAJ
author María Hijosa-Valsero
Jerson Garita-Cambronero
Ana I. Paniagua-García
Rebeca Díez-Antolínez
spellingShingle María Hijosa-Valsero
Jerson Garita-Cambronero
Ana I. Paniagua-García
Rebeca Díez-Antolínez
Biobutanol production from coffee silverskin
Microbial Cell Factories
Coffee silverskin
Lignocellulosic wastes
Pretreatment
Butanol
ABE fermentation
Biorefinery
author_facet María Hijosa-Valsero
Jerson Garita-Cambronero
Ana I. Paniagua-García
Rebeca Díez-Antolínez
author_sort María Hijosa-Valsero
title Biobutanol production from coffee silverskin
title_short 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_sort biobutanol production from coffee silverskin
publisher BMC
series Microbial Cell Factories
issn 1475-2859
publishDate 2018-09-01
description Abstract 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 gB/gS 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 CaCO3 concentration).
topic Coffee silverskin
Lignocellulosic wastes
Pretreatment
Butanol
ABE fermentation
Biorefinery
url http://link.springer.com/article/10.1186/s12934-018-1002-z
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