Kinetic Study of the Acid Post-hydrolysis of Xylooligosaccharides from Hydrothermal Pretreatment
Hydrothermal pretreatment of sugarcane bagasse is a water-based and environment-friendly process that results in almost complete hemicellulose solubilization in oligomeric form as xylooligossacharides (XOs). However, the soluble XOs cannot be utilized by microorganisms such as yeasts, and therefore,...
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description | Hydrothermal pretreatment of sugarcane bagasse is a water-based and environment-friendly process that results in almost complete hemicellulose solubilization in oligomeric form as xylooligossacharides (XOs). However, the soluble XOs cannot be utilized by microorganisms such as yeasts, and therefore, a further break down is necessary to generate pentose (C5) monomers that can be then biotransformed into ethanol or other metabolites. The kinetics of XOs post-hydrolysis with sulfuric, maleic, and oxalic acids (the latter two being dicarboxylic acids) in a sugarcane bagasse hemicellulosic hydrolysate was assessed in a bench-scale reactor (2 L). By means of a 2
2
full factorial design with center point triplicate, acid mass loading and temperature were varied from 0.5 and 2.0% and from 120 to 150 °C, respectively. An irreversible first-order consecutive reaction model of the hydrolysis of XOs in liquid medium was employed. Based on an Arrhenius-type equation, a kinetic parameter estimation was performed with genetic algorithms and the Runge-Kutta methods. For the three acids, the calculated exponential factors,
A
0
n
(
n
= 1, 2, and 3), ranged from 10
12
to 10
15
min
−1
; the dimensionless parameters,
m
n
(
n
= 1, 2, and 3), ranged from 0.86 to 1.97; and the activation energies ranged from 89 to 129.8 kJ·mol
−1
. The model—developed at microscale—correctly described the observed XOs, C5, and furfural post-hydrolysis profiles in bench scale and proved the dicarboxylic acids were more selective towards post-hydrolysis by having slower kinetics than sulfuric acid. |
doi_str_mv | 10.1007/s12155-017-9864-1 |
format | Article |
fullrecord | <record><control><sourceid>gale_proqu</sourceid><recordid>TN_cdi_proquest_journals_1960505789</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><galeid>A712240295</galeid><sourcerecordid>A712240295</sourcerecordid><originalsourceid>FETCH-LOGICAL-c383t-4ac618e629e03d1823f3030ec6d5e764527758665555db562ed5d056f20f86a93</originalsourceid><addsrcrecordid>eNp1kU1LxDAQhoso-PkDvBU8VydJk7bHRfxCQUEFbzEmk91I22iSPfTfm2VFVtDMIWHyPJPAWxTHBE4JQHMWCSWcV0CaqmtFXZGtYo90rKsIren2z5nVu8V-jO8AAmro9orXWzdicrp8TEszld6WaYHlTDtTPviYqsVkgu-n6OLq7mXqve_d3Eel9UIFZzCWNvihvF5xWQ2D6suHgCmgSgOO6bDYsaqPePS9HxTPlxdP59fV3f3VzfnsrtKsZamqlRakRUE7BGZIS5llwAC1MBwbUXPaNLwVgudl3rigaLgBLiwF2wrVsYPiZD33I_jPJcYk3_0yjPlJSToBHHjTblBz1aN0o_UpKD24qOWsIZTWQDueqdM_qFwGB6f9iNbl_i-BrAUdfIwBrfwIblBhkgTkKh-5zkfmfOQqH0myQ9dOzOw4x7Dx4X-lL8DSkS4</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>1960505789</pqid></control><display><type>article</type><title>Kinetic Study of the Acid Post-hydrolysis of Xylooligosaccharides from Hydrothermal Pretreatment</title><source>SpringerLink Journals</source><creator>Nakasu, P. Y. S. ; Chagas, M. F. ; Costa, A. C. ; Rabelo, S. C.</creator><creatorcontrib>Nakasu, P. Y. S. ; Chagas, M. F. ; Costa, A. C. ; Rabelo, S. C.</creatorcontrib><description>Hydrothermal pretreatment of sugarcane bagasse is a water-based and environment-friendly process that results in almost complete hemicellulose solubilization in oligomeric form as xylooligossacharides (XOs). However, the soluble XOs cannot be utilized by microorganisms such as yeasts, and therefore, a further break down is necessary to generate pentose (C5) monomers that can be then biotransformed into ethanol or other metabolites. The kinetics of XOs post-hydrolysis with sulfuric, maleic, and oxalic acids (the latter two being dicarboxylic acids) in a sugarcane bagasse hemicellulosic hydrolysate was assessed in a bench-scale reactor (2 L). By means of a 2
2
full factorial design with center point triplicate, acid mass loading and temperature were varied from 0.5 and 2.0% and from 120 to 150 °C, respectively. An irreversible first-order consecutive reaction model of the hydrolysis of XOs in liquid medium was employed. Based on an Arrhenius-type equation, a kinetic parameter estimation was performed with genetic algorithms and the Runge-Kutta methods. For the three acids, the calculated exponential factors,
A
0
n
(
n
= 1, 2, and 3), ranged from 10
12
to 10
15
min
−1
; the dimensionless parameters,
m
n
(
n
= 1, 2, and 3), ranged from 0.86 to 1.97; and the activation energies ranged from 89 to 129.8 kJ·mol
−1
. The model—developed at microscale—correctly described the observed XOs, C5, and furfural post-hydrolysis profiles in bench scale and proved the dicarboxylic acids were more selective towards post-hydrolysis by having slower kinetics than sulfuric acid.</description><identifier>ISSN: 1939-1234</identifier><identifier>EISSN: 1939-1242</identifier><identifier>DOI: 10.1007/s12155-017-9864-1</identifier><language>eng</language><publisher>New York: Springer US</publisher><subject>Acids ; Analysis ; Bagasse ; Biomedical and Life Sciences ; Breaking down ; Dicarboxylic acids ; Ethanol ; Factorial design ; Furfural ; Genetic algorithms ; Hemicellulose ; Hydrolysis ; Hydrothermal pretreatment ; Kinetics ; Life Sciences ; Metabolites ; Microorganisms ; Monomers ; Monosaccharides ; Oxalic acid ; Parameter estimation ; Pentose ; Plant Breeding/Biotechnology ; Plant Ecology ; Plant Genetics and Genomics ; Plant Sciences ; Reaction kinetics ; Runge-Kutta method ; Solubilization ; Sugarcane ; Sugars ; Sulfur ; Sulfuric acid ; Wood Science & Technology ; Yeasts</subject><ispartof>Bioenergy research, 2017-12, Vol.10 (4), p.1045-1056</ispartof><rights>Springer Science+Business Media, LLC 2017</rights><rights>COPYRIGHT 2017 Springer</rights><rights>Bioenergy Research is a copyright of Springer, 2017.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c383t-4ac618e629e03d1823f3030ec6d5e764527758665555db562ed5d056f20f86a93</citedby><cites>FETCH-LOGICAL-c383t-4ac618e629e03d1823f3030ec6d5e764527758665555db562ed5d056f20f86a93</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://link.springer.com/content/pdf/10.1007/s12155-017-9864-1$$EPDF$$P50$$Gspringer$$H</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1007/s12155-017-9864-1$$EHTML$$P50$$Gspringer$$H</linktohtml><link.rule.ids>314,776,780,27901,27902,41464,42533,51294</link.rule.ids></links><search><creatorcontrib>Nakasu, P. Y. S.</creatorcontrib><creatorcontrib>Chagas, M. F.</creatorcontrib><creatorcontrib>Costa, A. C.</creatorcontrib><creatorcontrib>Rabelo, S. C.</creatorcontrib><title>Kinetic Study of the Acid Post-hydrolysis of Xylooligosaccharides from Hydrothermal Pretreatment</title><title>Bioenergy research</title><addtitle>Bioenerg. Res</addtitle><description>Hydrothermal pretreatment of sugarcane bagasse is a water-based and environment-friendly process that results in almost complete hemicellulose solubilization in oligomeric form as xylooligossacharides (XOs). However, the soluble XOs cannot be utilized by microorganisms such as yeasts, and therefore, a further break down is necessary to generate pentose (C5) monomers that can be then biotransformed into ethanol or other metabolites. The kinetics of XOs post-hydrolysis with sulfuric, maleic, and oxalic acids (the latter two being dicarboxylic acids) in a sugarcane bagasse hemicellulosic hydrolysate was assessed in a bench-scale reactor (2 L). By means of a 2
2
full factorial design with center point triplicate, acid mass loading and temperature were varied from 0.5 and 2.0% and from 120 to 150 °C, respectively. An irreversible first-order consecutive reaction model of the hydrolysis of XOs in liquid medium was employed. Based on an Arrhenius-type equation, a kinetic parameter estimation was performed with genetic algorithms and the Runge-Kutta methods. For the three acids, the calculated exponential factors,
A
0
n
(
n
= 1, 2, and 3), ranged from 10
12
to 10
15
min
−1
; the dimensionless parameters,
m
n
(
n
= 1, 2, and 3), ranged from 0.86 to 1.97; and the activation energies ranged from 89 to 129.8 kJ·mol
−1
. The model—developed at microscale—correctly described the observed XOs, C5, and furfural post-hydrolysis profiles in bench scale and proved the dicarboxylic acids were more selective towards post-hydrolysis by having slower kinetics than sulfuric acid.</description><subject>Acids</subject><subject>Analysis</subject><subject>Bagasse</subject><subject>Biomedical and Life Sciences</subject><subject>Breaking down</subject><subject>Dicarboxylic acids</subject><subject>Ethanol</subject><subject>Factorial design</subject><subject>Furfural</subject><subject>Genetic algorithms</subject><subject>Hemicellulose</subject><subject>Hydrolysis</subject><subject>Hydrothermal pretreatment</subject><subject>Kinetics</subject><subject>Life Sciences</subject><subject>Metabolites</subject><subject>Microorganisms</subject><subject>Monomers</subject><subject>Monosaccharides</subject><subject>Oxalic acid</subject><subject>Parameter estimation</subject><subject>Pentose</subject><subject>Plant Breeding/Biotechnology</subject><subject>Plant Ecology</subject><subject>Plant Genetics and Genomics</subject><subject>Plant Sciences</subject><subject>Reaction kinetics</subject><subject>Runge-Kutta method</subject><subject>Solubilization</subject><subject>Sugarcane</subject><subject>Sugars</subject><subject>Sulfur</subject><subject>Sulfuric acid</subject><subject>Wood Science & Technology</subject><subject>Yeasts</subject><issn>1939-1234</issn><issn>1939-1242</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2017</creationdate><recordtype>article</recordtype><sourceid>BENPR</sourceid><recordid>eNp1kU1LxDAQhoso-PkDvBU8VydJk7bHRfxCQUEFbzEmk91I22iSPfTfm2VFVtDMIWHyPJPAWxTHBE4JQHMWCSWcV0CaqmtFXZGtYo90rKsIren2z5nVu8V-jO8AAmro9orXWzdicrp8TEszld6WaYHlTDtTPviYqsVkgu-n6OLq7mXqve_d3Eel9UIFZzCWNvihvF5xWQ2D6suHgCmgSgOO6bDYsaqPePS9HxTPlxdP59fV3f3VzfnsrtKsZamqlRakRUE7BGZIS5llwAC1MBwbUXPaNLwVgudl3rigaLgBLiwF2wrVsYPiZD33I_jPJcYk3_0yjPlJSToBHHjTblBz1aN0o_UpKD24qOWsIZTWQDueqdM_qFwGB6f9iNbl_i-BrAUdfIwBrfwIblBhkgTkKh-5zkfmfOQqH0myQ9dOzOw4x7Dx4X-lL8DSkS4</recordid><startdate>20171201</startdate><enddate>20171201</enddate><creator>Nakasu, P. 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Y. S. ; Chagas, M. F. ; Costa, A. C. ; Rabelo, S. C.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c383t-4ac618e629e03d1823f3030ec6d5e764527758665555db562ed5d056f20f86a93</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2017</creationdate><topic>Acids</topic><topic>Analysis</topic><topic>Bagasse</topic><topic>Biomedical and Life Sciences</topic><topic>Breaking down</topic><topic>Dicarboxylic acids</topic><topic>Ethanol</topic><topic>Factorial design</topic><topic>Furfural</topic><topic>Genetic algorithms</topic><topic>Hemicellulose</topic><topic>Hydrolysis</topic><topic>Hydrothermal pretreatment</topic><topic>Kinetics</topic><topic>Life Sciences</topic><topic>Metabolites</topic><topic>Microorganisms</topic><topic>Monomers</topic><topic>Monosaccharides</topic><topic>Oxalic acid</topic><topic>Parameter estimation</topic><topic>Pentose</topic><topic>Plant Breeding/Biotechnology</topic><topic>Plant Ecology</topic><topic>Plant Genetics and Genomics</topic><topic>Plant Sciences</topic><topic>Reaction kinetics</topic><topic>Runge-Kutta method</topic><topic>Solubilization</topic><topic>Sugarcane</topic><topic>Sugars</topic><topic>Sulfur</topic><topic>Sulfuric acid</topic><topic>Wood Science & Technology</topic><topic>Yeasts</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Nakasu, P. Y. S.</creatorcontrib><creatorcontrib>Chagas, M. F.</creatorcontrib><creatorcontrib>Costa, A. C.</creatorcontrib><creatorcontrib>Rabelo, S. 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Y. S.</au><au>Chagas, M. F.</au><au>Costa, A. C.</au><au>Rabelo, S. C.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Kinetic Study of the Acid Post-hydrolysis of Xylooligosaccharides from Hydrothermal Pretreatment</atitle><jtitle>Bioenergy research</jtitle><stitle>Bioenerg. Res</stitle><date>2017-12-01</date><risdate>2017</risdate><volume>10</volume><issue>4</issue><spage>1045</spage><epage>1056</epage><pages>1045-1056</pages><issn>1939-1234</issn><eissn>1939-1242</eissn><abstract>Hydrothermal pretreatment of sugarcane bagasse is a water-based and environment-friendly process that results in almost complete hemicellulose solubilization in oligomeric form as xylooligossacharides (XOs). However, the soluble XOs cannot be utilized by microorganisms such as yeasts, and therefore, a further break down is necessary to generate pentose (C5) monomers that can be then biotransformed into ethanol or other metabolites. The kinetics of XOs post-hydrolysis with sulfuric, maleic, and oxalic acids (the latter two being dicarboxylic acids) in a sugarcane bagasse hemicellulosic hydrolysate was assessed in a bench-scale reactor (2 L). By means of a 2
2
full factorial design with center point triplicate, acid mass loading and temperature were varied from 0.5 and 2.0% and from 120 to 150 °C, respectively. An irreversible first-order consecutive reaction model of the hydrolysis of XOs in liquid medium was employed. Based on an Arrhenius-type equation, a kinetic parameter estimation was performed with genetic algorithms and the Runge-Kutta methods. For the three acids, the calculated exponential factors,
A
0
n
(
n
= 1, 2, and 3), ranged from 10
12
to 10
15
min
−1
; the dimensionless parameters,
m
n
(
n
= 1, 2, and 3), ranged from 0.86 to 1.97; and the activation energies ranged from 89 to 129.8 kJ·mol
−1
. The model—developed at microscale—correctly described the observed XOs, C5, and furfural post-hydrolysis profiles in bench scale and proved the dicarboxylic acids were more selective towards post-hydrolysis by having slower kinetics than sulfuric acid.</abstract><cop>New York</cop><pub>Springer US</pub><doi>10.1007/s12155-017-9864-1</doi><tpages>12</tpages></addata></record> |
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subjects | Acids Analysis Bagasse Biomedical and Life Sciences Breaking down Dicarboxylic acids Ethanol Factorial design Furfural Genetic algorithms Hemicellulose Hydrolysis Hydrothermal pretreatment Kinetics Life Sciences Metabolites Microorganisms Monomers Monosaccharides Oxalic acid Parameter estimation Pentose Plant Breeding/Biotechnology Plant Ecology Plant Genetics and Genomics Plant Sciences Reaction kinetics Runge-Kutta method Solubilization Sugarcane Sugars Sulfur Sulfuric acid Wood Science & Technology Yeasts |
title | Kinetic Study of the Acid Post-hydrolysis of Xylooligosaccharides from Hydrothermal Pretreatment |
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