Corn Stover Pretreatment with Na<sub>2</sub>CO<sub>3</sub> Solution from Absorption of Recovered CO<sub>2</sub>

Renewable resources such as lignocellulosic biomass are effective at producing fermentable sugars during enzymatic hydrolysis when pretreated. Optimizing pretreatment methods for delignification while maintaining sustainability and low processing costs requires innovative strategies such as reusing...

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Main Authors: Valerie García-Negrón, Matthew J. Toht
Format: Article
Language:English
Published: MDPI AG 2022-11-01
Series:Fermentation
Subjects:
Online Access:https://www.mdpi.com/2311-5637/8/11/600
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author Valerie García-Negrón
Matthew J. Toht
author_facet Valerie García-Negrón
Matthew J. Toht
author_sort Valerie García-Negrón
collection DOAJ
description Renewable resources such as lignocellulosic biomass are effective at producing fermentable sugars during enzymatic hydrolysis when pretreated. Optimizing pretreatment methods for delignification while maintaining sustainability and low processing costs requires innovative strategies such as reusing greenhouse gas emissions for materials processing. Corn stover, an agricultural waste residue, was pretreated with 2.2 M <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><mrow><mi mathvariant="normal">N</mi><msub><mi mathvariant="normal">a</mi><mn>2</mn></msub><mi mathvariant="normal">C</mi><msub><mi mathvariant="normal">O</mi><mn>3</mn></msub></mrow></semantics></math></inline-formula> produced from <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><mrow><mi mathvariant="normal">C</mi><msub><mi mathvariant="normal">O</mi><mn>2</mn></msub></mrow></semantics></math></inline-formula> captured via absorption in a 5 M NaOH solution. Composition analysis of the pretreated corn stover exhibited higher cellulose content (40.96%) and less lignin (16.50%) than the untreated biomass. Changes in the chemical structures are visible in the FTIR-ATR spectra, particularly in the cellulose and lignin-related absorption bands. The sugar release from hydrolysis was evaluated at different time intervals and by varying two enzyme ratios of CTec2-to-HTec2 (2:1 and 3:1). Enzymatic hydrolysis produced higher and more stable glucose yields for the pretreated biomass, surpassing 90% after 24 h using the 3:1 enzyme ratio. Sugar concentrations notably increased after pretreatment and even more when using the cellulase-rich enzyme solution. The maximum glucose, xylose, and arabinose recovered were 44, 19, and 2.3 <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><mrow><mi mathvariant="normal">g</mi><mo> </mo><mi mathvariant="normal">L</mi></mrow></semantics></math></inline-formula><sup>−1</sup>. These results demonstrate the viability of capturing <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><mrow><mi mathvariant="normal">C</mi><msub><mi mathvariant="normal">O</mi><mn>2</mn></msub></mrow></semantics></math></inline-formula> and converting it into an efficient <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><mrow><mi mathvariant="normal">N</mi><msub><mi mathvariant="normal">a</mi><mn>2</mn></msub><mi mathvariant="normal">C</mi><msub><mi mathvariant="normal">O</mi><mn>3</mn></msub></mrow></semantics></math></inline-formula> pretreatment for corn stover biomass. Additional processing optimizations depend on the combination of physicochemical parameters selected.
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spelling doaj.art-65bbeaff7a594dcbb32ab77b987009612023-11-24T04:38:05ZengMDPI AGFermentation2311-56372022-11-0181160010.3390/fermentation8110600Corn Stover Pretreatment with Na<sub>2</sub>CO<sub>3</sub> Solution from Absorption of Recovered CO<sub>2</sub>Valerie García-Negrón0Matthew J. Toht1Eastern Regional Research Center, Agricultural Research Service, U.S. Department of Agriculture, 600 East Mermaid Lane, Wyndmoor, PA 19038, USAEastern Regional Research Center, Agricultural Research Service, U.S. Department of Agriculture, 600 East Mermaid Lane, Wyndmoor, PA 19038, USARenewable resources such as lignocellulosic biomass are effective at producing fermentable sugars during enzymatic hydrolysis when pretreated. Optimizing pretreatment methods for delignification while maintaining sustainability and low processing costs requires innovative strategies such as reusing greenhouse gas emissions for materials processing. Corn stover, an agricultural waste residue, was pretreated with 2.2 M <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><mrow><mi mathvariant="normal">N</mi><msub><mi mathvariant="normal">a</mi><mn>2</mn></msub><mi mathvariant="normal">C</mi><msub><mi mathvariant="normal">O</mi><mn>3</mn></msub></mrow></semantics></math></inline-formula> produced from <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><mrow><mi mathvariant="normal">C</mi><msub><mi mathvariant="normal">O</mi><mn>2</mn></msub></mrow></semantics></math></inline-formula> captured via absorption in a 5 M NaOH solution. Composition analysis of the pretreated corn stover exhibited higher cellulose content (40.96%) and less lignin (16.50%) than the untreated biomass. Changes in the chemical structures are visible in the FTIR-ATR spectra, particularly in the cellulose and lignin-related absorption bands. The sugar release from hydrolysis was evaluated at different time intervals and by varying two enzyme ratios of CTec2-to-HTec2 (2:1 and 3:1). Enzymatic hydrolysis produced higher and more stable glucose yields for the pretreated biomass, surpassing 90% after 24 h using the 3:1 enzyme ratio. Sugar concentrations notably increased after pretreatment and even more when using the cellulase-rich enzyme solution. The maximum glucose, xylose, and arabinose recovered were 44, 19, and 2.3 <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><mrow><mi mathvariant="normal">g</mi><mo> </mo><mi mathvariant="normal">L</mi></mrow></semantics></math></inline-formula><sup>−1</sup>. These results demonstrate the viability of capturing <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><mrow><mi mathvariant="normal">C</mi><msub><mi mathvariant="normal">O</mi><mn>2</mn></msub></mrow></semantics></math></inline-formula> and converting it into an efficient <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><mrow><mi mathvariant="normal">N</mi><msub><mi mathvariant="normal">a</mi><mn>2</mn></msub><mi mathvariant="normal">C</mi><msub><mi mathvariant="normal">O</mi><mn>3</mn></msub></mrow></semantics></math></inline-formula> pretreatment for corn stover biomass. Additional processing optimizations depend on the combination of physicochemical parameters selected.https://www.mdpi.com/2311-5637/8/11/600corn stovercarbon dioxide absorptionbiomass pretreatmentsodium carbonatesodium hydroxide
spellingShingle Valerie García-Negrón
Matthew J. Toht
Corn Stover Pretreatment with Na<sub>2</sub>CO<sub>3</sub> Solution from Absorption of Recovered CO<sub>2</sub>
Fermentation
corn stover
carbon dioxide absorption
biomass pretreatment
sodium carbonate
sodium hydroxide
title Corn Stover Pretreatment with Na<sub>2</sub>CO<sub>3</sub> Solution from Absorption of Recovered CO<sub>2</sub>
title_full Corn Stover Pretreatment with Na<sub>2</sub>CO<sub>3</sub> Solution from Absorption of Recovered CO<sub>2</sub>
title_fullStr Corn Stover Pretreatment with Na<sub>2</sub>CO<sub>3</sub> Solution from Absorption of Recovered CO<sub>2</sub>
title_full_unstemmed Corn Stover Pretreatment with Na<sub>2</sub>CO<sub>3</sub> Solution from Absorption of Recovered CO<sub>2</sub>
title_short Corn Stover Pretreatment with Na<sub>2</sub>CO<sub>3</sub> Solution from Absorption of Recovered CO<sub>2</sub>
title_sort corn stover pretreatment with na sub 2 sub co sub 3 sub solution from absorption of recovered co sub 2 sub
topic corn stover
carbon dioxide absorption
biomass pretreatment
sodium carbonate
sodium hydroxide
url https://www.mdpi.com/2311-5637/8/11/600
work_keys_str_mv AT valeriegarcianegron cornstoverpretreatmentwithnasub2subcosub3subsolutionfromabsorptionofrecoveredcosub2sub
AT matthewjtoht cornstoverpretreatmentwithnasub2subcosub3subsolutionfromabsorptionofrecoveredcosub2sub