Comparison between liquid and solid acids catalysts on reducing sugars conversion from furfural residues via pretreatments
The effect of liquid and solid acids catalysts on reducing sugar yields via different pretreatments of furfural residues. •Furfural residues conversion into reducing sugars was researched.•Yields of liquid and solid acids are over 60% and 30%, respectively.•TOF for liquid acid is about 4–5 times of...
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creator | Lin, Keying Ma, Baojun Sun, Yuan Liu, Wanyi |
description | The effect of liquid and solid acids catalysts on reducing sugar yields via different pretreatments of furfural residues.
•Furfural residues conversion into reducing sugars was researched.•Yields of liquid and solid acids are over 60% and 30%, respectively.•TOF for liquid acid is about 4–5 times of that for solid acids.•Liquid acid is extremely efficient.•Solid acids are green and reusable.
Liquid sulphuric acid is adopted and compared with carbon-based sulfonated solid acids (coal tar-based and active carbon-based) for furfural residues conversion into reducing sugars. The optimum hydrolysis conditions of liquid acid are at 4% of sulphuric acid, 25:1 of liquid and solid ratio, 175°C of reaction temperature and 120min of reaction time. The reducing sugar yields are reached over 60% on liquid acid via NaOH/H2O2, NaOH/microwave and NaOH/ultrasonic pretreatments, whereas only over 30% on solid acids. The TOFs (turnover number frequency) via NaOH/H2O2 pretreatments are 0.093, 0.020 and 0.023h−1 for liquid sulphuric acid, coal tar-based and active carbon-based solid acids catalysts, respectively. Considering the efficiency, cost and environment factors, the liquid and solid acids have their own advantages of potential commercial application values. |
doi_str_mv | 10.1016/j.biortech.2014.06.022 |
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•Furfural residues conversion into reducing sugars was researched.•Yields of liquid and solid acids are over 60% and 30%, respectively.•TOF for liquid acid is about 4–5 times of that for solid acids.•Liquid acid is extremely efficient.•Solid acids are green and reusable.
Liquid sulphuric acid is adopted and compared with carbon-based sulfonated solid acids (coal tar-based and active carbon-based) for furfural residues conversion into reducing sugars. The optimum hydrolysis conditions of liquid acid are at 4% of sulphuric acid, 25:1 of liquid and solid ratio, 175°C of reaction temperature and 120min of reaction time. The reducing sugar yields are reached over 60% on liquid acid via NaOH/H2O2, NaOH/microwave and NaOH/ultrasonic pretreatments, whereas only over 30% on solid acids. The TOFs (turnover number frequency) via NaOH/H2O2 pretreatments are 0.093, 0.020 and 0.023h−1 for liquid sulphuric acid, coal tar-based and active carbon-based solid acids catalysts, respectively. Considering the efficiency, cost and environment factors, the liquid and solid acids have their own advantages of potential commercial application values.</description><identifier>ISSN: 0960-8524</identifier><identifier>EISSN: 1873-2976</identifier><identifier>DOI: 10.1016/j.biortech.2014.06.022</identifier><identifier>PMID: 24976491</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Biological and medical sciences ; Carbohydrates - chemistry ; Catalysis ; Catalysis - drug effects ; Coal ; Conversion ; Fundamental and applied biological sciences. Psychology ; Furaldehyde - metabolism ; Furfural residues ; Hydrolysis - drug effects ; Liquid acid ; Liquids ; Pretreatment ; Reducing sugars ; Residues ; Solid acid ; Sugars ; Sulfuric acid ; Sulfuric Acids - pharmacology ; Temperature ; Time Factors</subject><ispartof>Bioresource technology, 2014-09, Vol.167, p.133-136</ispartof><rights>2014 Elsevier Ltd</rights><rights>2015 INIST-CNRS</rights><rights>Copyright © 2014 Elsevier Ltd. All rights reserved.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c431t-6d7b6788e29af691ca2514ef821780f3f0abc12c41edc8986157bfdd9733c3193</citedby><cites>FETCH-LOGICAL-c431t-6d7b6788e29af691ca2514ef821780f3f0abc12c41edc8986157bfdd9733c3193</cites><orcidid>0000-0003-0020-6650</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.biortech.2014.06.022$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3548,27923,27924,45994</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=28615517$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/24976491$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Lin, Keying</creatorcontrib><creatorcontrib>Ma, Baojun</creatorcontrib><creatorcontrib>Sun, Yuan</creatorcontrib><creatorcontrib>Liu, Wanyi</creatorcontrib><title>Comparison between liquid and solid acids catalysts on reducing sugars conversion from furfural residues via pretreatments</title><title>Bioresource technology</title><addtitle>Bioresour Technol</addtitle><description>The effect of liquid and solid acids catalysts on reducing sugar yields via different pretreatments of furfural residues.
•Furfural residues conversion into reducing sugars was researched.•Yields of liquid and solid acids are over 60% and 30%, respectively.•TOF for liquid acid is about 4–5 times of that for solid acids.•Liquid acid is extremely efficient.•Solid acids are green and reusable.
Liquid sulphuric acid is adopted and compared with carbon-based sulfonated solid acids (coal tar-based and active carbon-based) for furfural residues conversion into reducing sugars. The optimum hydrolysis conditions of liquid acid are at 4% of sulphuric acid, 25:1 of liquid and solid ratio, 175°C of reaction temperature and 120min of reaction time. The reducing sugar yields are reached over 60% on liquid acid via NaOH/H2O2, NaOH/microwave and NaOH/ultrasonic pretreatments, whereas only over 30% on solid acids. The TOFs (turnover number frequency) via NaOH/H2O2 pretreatments are 0.093, 0.020 and 0.023h−1 for liquid sulphuric acid, coal tar-based and active carbon-based solid acids catalysts, respectively. Considering the efficiency, cost and environment factors, the liquid and solid acids have their own advantages of potential commercial application values.</description><subject>Biological and medical sciences</subject><subject>Carbohydrates - chemistry</subject><subject>Catalysis</subject><subject>Catalysis - drug effects</subject><subject>Coal</subject><subject>Conversion</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>Furaldehyde - metabolism</subject><subject>Furfural residues</subject><subject>Hydrolysis - drug effects</subject><subject>Liquid acid</subject><subject>Liquids</subject><subject>Pretreatment</subject><subject>Reducing sugars</subject><subject>Residues</subject><subject>Solid acid</subject><subject>Sugars</subject><subject>Sulfuric acid</subject><subject>Sulfuric Acids - pharmacology</subject><subject>Temperature</subject><subject>Time Factors</subject><issn>0960-8524</issn><issn>1873-2976</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2014</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><recordid>eNqNkVGP1CAQgInReHurf-HCi4kvrQy0tH3TbNQzucQXfSYUhpNNW_aArjl_vWx2Tx81ITDJfAMzfITcAKuBgXy3r0cfYkbzo-YMmprJmnH-jGyg70TFh04-Jxs2SFb1LW-uyHVKe8aYgI6_JFe8KUAzwIb82oX5oKNPYaEj5p-IC538w-ot1YulKUynyHibqNFZT48pJ1rYiHY1frmnab3XsSTDcsSYfEm5GGbq1liWngqYvF0x0aPX9BAxR9R5xiWnV-SF01PC15dzS75_-vhtd1vdff38ZffhrjKNgFxJ242y63vkg3ZyAKN5Cw26nkPXMycc06MBbhpAa_qhl9B2o7N26IQwAgaxJW_P9x5ieCidZDX7ZHCa9IJhTQpayQDY0Db_gTa9FIMo25bIM2piSCmiU4foZx0fFTB1UqT26kmROilSTKqiqBTeXN5Yxxntn7InJwV4cwF0MnpyUS_Gp7_cacIWusK9P3NYPu_oMapkPC4GrY9osrLB_6uX3-WutTA</recordid><startdate>20140901</startdate><enddate>20140901</enddate><creator>Lin, Keying</creator><creator>Ma, Baojun</creator><creator>Sun, Yuan</creator><creator>Liu, Wanyi</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>CGR</scope><scope>CUY</scope><scope>CVF</scope><scope>ECM</scope><scope>EIF</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7X8</scope><scope>7SU</scope><scope>7TB</scope><scope>8FD</scope><scope>C1K</scope><scope>FR3</scope><scope>KR7</scope><orcidid>https://orcid.org/0000-0003-0020-6650</orcidid></search><sort><creationdate>20140901</creationdate><title>Comparison between liquid and solid acids catalysts on reducing sugars conversion from furfural residues via pretreatments</title><author>Lin, Keying ; Ma, Baojun ; Sun, Yuan ; Liu, Wanyi</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c431t-6d7b6788e29af691ca2514ef821780f3f0abc12c41edc8986157bfdd9733c3193</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2014</creationdate><topic>Biological and medical sciences</topic><topic>Carbohydrates - chemistry</topic><topic>Catalysis</topic><topic>Catalysis - drug effects</topic><topic>Coal</topic><topic>Conversion</topic><topic>Fundamental and applied biological sciences. Psychology</topic><topic>Furaldehyde - metabolism</topic><topic>Furfural residues</topic><topic>Hydrolysis - drug effects</topic><topic>Liquid acid</topic><topic>Liquids</topic><topic>Pretreatment</topic><topic>Reducing sugars</topic><topic>Residues</topic><topic>Solid acid</topic><topic>Sugars</topic><topic>Sulfuric acid</topic><topic>Sulfuric Acids - pharmacology</topic><topic>Temperature</topic><topic>Time Factors</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Lin, Keying</creatorcontrib><creatorcontrib>Ma, Baojun</creatorcontrib><creatorcontrib>Sun, Yuan</creatorcontrib><creatorcontrib>Liu, Wanyi</creatorcontrib><collection>Pascal-Francis</collection><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>MEDLINE - Academic</collection><collection>Environmental Engineering Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><jtitle>Bioresource technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Lin, Keying</au><au>Ma, Baojun</au><au>Sun, Yuan</au><au>Liu, Wanyi</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Comparison between liquid and solid acids catalysts on reducing sugars conversion from furfural residues via pretreatments</atitle><jtitle>Bioresource technology</jtitle><addtitle>Bioresour Technol</addtitle><date>2014-09-01</date><risdate>2014</risdate><volume>167</volume><spage>133</spage><epage>136</epage><pages>133-136</pages><issn>0960-8524</issn><eissn>1873-2976</eissn><abstract>The effect of liquid and solid acids catalysts on reducing sugar yields via different pretreatments of furfural residues.
•Furfural residues conversion into reducing sugars was researched.•Yields of liquid and solid acids are over 60% and 30%, respectively.•TOF for liquid acid is about 4–5 times of that for solid acids.•Liquid acid is extremely efficient.•Solid acids are green and reusable.
Liquid sulphuric acid is adopted and compared with carbon-based sulfonated solid acids (coal tar-based and active carbon-based) for furfural residues conversion into reducing sugars. The optimum hydrolysis conditions of liquid acid are at 4% of sulphuric acid, 25:1 of liquid and solid ratio, 175°C of reaction temperature and 120min of reaction time. The reducing sugar yields are reached over 60% on liquid acid via NaOH/H2O2, NaOH/microwave and NaOH/ultrasonic pretreatments, whereas only over 30% on solid acids. The TOFs (turnover number frequency) via NaOH/H2O2 pretreatments are 0.093, 0.020 and 0.023h−1 for liquid sulphuric acid, coal tar-based and active carbon-based solid acids catalysts, respectively. Considering the efficiency, cost and environment factors, the liquid and solid acids have their own advantages of potential commercial application values.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><pmid>24976491</pmid><doi>10.1016/j.biortech.2014.06.022</doi><tpages>4</tpages><orcidid>https://orcid.org/0000-0003-0020-6650</orcidid></addata></record> |
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subjects | Biological and medical sciences Carbohydrates - chemistry Catalysis Catalysis - drug effects Coal Conversion Fundamental and applied biological sciences. Psychology Furaldehyde - metabolism Furfural residues Hydrolysis - drug effects Liquid acid Liquids Pretreatment Reducing sugars Residues Solid acid Sugars Sulfuric acid Sulfuric Acids - pharmacology Temperature Time Factors |
title | Comparison between liquid and solid acids catalysts on reducing sugars conversion from furfural residues via pretreatments |
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