An Acidic Two-Step Hydrothermal Process To Enhance Acetic Acid Production from Carbohydrate Biomass
An acidic two-step hydrothermal process to improve acetic acid production was investigated. In the first-step reaction, levulinic acid is formed in the presence of an acid catalyst. In the second-step reaction, the levulinic acid is converted into acetic acid via oxidation with newly supplied oxygen...
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Veröffentlicht in: | Industrial & engineering chemistry research 2012-03, Vol.51 (12), p.4759-4763 |
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description | An acidic two-step hydrothermal process to improve acetic acid production was investigated. In the first-step reaction, levulinic acid is formed in the presence of an acid catalyst. In the second-step reaction, the levulinic acid is converted into acetic acid via oxidation with newly supplied oxygen. The acetic acid yield from this two-step process was much higher than that without the acid catalysts in the first step. The acetic acid yield reached 23% with a purity of 47% from glucose and 26% with a purity of 52% from fructose. These yields were achieved at a reaction temperature of 523 K, a reaction time of 300 s, and pH 0.5 with HCl as an acid catalyst for the first step and at a reaction temperature of 523 K, a reaction time of 60 s, and an oxygen supply of 100% for the second step. |
doi_str_mv | 10.1021/ie202506c |
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In the first-step reaction, levulinic acid is formed in the presence of an acid catalyst. In the second-step reaction, the levulinic acid is converted into acetic acid via oxidation with newly supplied oxygen. The acetic acid yield from this two-step process was much higher than that without the acid catalysts in the first step. The acetic acid yield reached 23% with a purity of 47% from glucose and 26% with a purity of 52% from fructose. These yields were achieved at a reaction temperature of 523 K, a reaction time of 300 s, and pH 0.5 with HCl as an acid catalyst for the first step and at a reaction temperature of 523 K, a reaction time of 60 s, and an oxygen supply of 100% for the second step.</description><identifier>ISSN: 0888-5885</identifier><identifier>EISSN: 1520-5045</identifier><identifier>DOI: 10.1021/ie202506c</identifier><identifier>CODEN: IECRED</identifier><language>eng</language><publisher>Washington, DC: American Chemical Society</publisher><subject>Acetic acid ; Applied sciences ; Carbohydrates ; Catalysts ; Chemical engineering ; Exact sciences and technology ; Fructose ; Glucose ; Industrial engineering ; Purity ; Reaction time</subject><ispartof>Industrial & engineering chemistry research, 2012-03, Vol.51 (12), p.4759-4763</ispartof><rights>Copyright © 2012 American Chemical Society</rights><rights>2015 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a388t-c4b6862185850fd08092f5b4984d0c60bf2ede812fd60fe0c9c392492137dadd3</citedby><cites>FETCH-LOGICAL-a388t-c4b6862185850fd08092f5b4984d0c60bf2ede812fd60fe0c9c392492137dadd3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://pubs.acs.org/doi/pdf/10.1021/ie202506c$$EPDF$$P50$$Gacs$$H</linktopdf><linktohtml>$$Uhttps://pubs.acs.org/doi/10.1021/ie202506c$$EHTML$$P50$$Gacs$$H</linktohtml><link.rule.ids>314,780,784,2765,27076,27924,27925,56738,56788</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=25720947$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Fang, Yan</creatorcontrib><creatorcontrib>Zeng, Xu</creatorcontrib><creatorcontrib>Yan, Peng</creatorcontrib><creatorcontrib>Jing, Zhenzi</creatorcontrib><creatorcontrib>Jin, Fangming</creatorcontrib><title>An Acidic Two-Step Hydrothermal Process To Enhance Acetic Acid Production from Carbohydrate Biomass</title><title>Industrial & engineering chemistry research</title><addtitle>Ind. 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These yields were achieved at a reaction temperature of 523 K, a reaction time of 300 s, and pH 0.5 with HCl as an acid catalyst for the first step and at a reaction temperature of 523 K, a reaction time of 60 s, and an oxygen supply of 100% for the second step.</description><subject>Acetic acid</subject><subject>Applied sciences</subject><subject>Carbohydrates</subject><subject>Catalysts</subject><subject>Chemical engineering</subject><subject>Exact sciences and technology</subject><subject>Fructose</subject><subject>Glucose</subject><subject>Industrial engineering</subject><subject>Purity</subject><subject>Reaction time</subject><issn>0888-5885</issn><issn>1520-5045</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2012</creationdate><recordtype>article</recordtype><recordid>eNptkE1LAzEURYMoWKsL_0E2gi5GXzLJNLOspVqhoGBdD5l80JSZSU0ySP-9U1rqxtVb3HMPvIvQLYFHApQ8OUOBcijUGRoRTiHjwPg5GoEQIuNC8Et0FeMGADhnbITUtMNT5bRTePXjs89ktnix08GntQmtbPBH8MrEiFcez7u17JQZeJMGfl_bx7pXyfkO2-BbPJOh9utBIJPBz863MsZrdGFlE83N8Y7R18t8NVtky_fXt9l0mclciJQpVheioERwwcFqEFBSy2tWCqZBFVBbarQRhFpdgDWgSpWXlJWU5BMttc7H6P7g3Qb_3ZuYqtZFZZpGdsb3sSJFSXOAgvABfTigKvgYg7HVNrhWhl1FoNoPWZ2GHNi7o1ZGJRsbhhFcPBUon1Ao2eSPkypWG9-Hbnj2H98vhFx90g</recordid><startdate>20120328</startdate><enddate>20120328</enddate><creator>Fang, Yan</creator><creator>Zeng, Xu</creator><creator>Yan, Peng</creator><creator>Jing, Zhenzi</creator><creator>Jin, Fangming</creator><general>American Chemical Society</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>7TB</scope><scope>8BQ</scope><scope>8FD</scope><scope>FR3</scope><scope>JG9</scope></search><sort><creationdate>20120328</creationdate><title>An Acidic Two-Step Hydrothermal Process To Enhance Acetic Acid Production from Carbohydrate Biomass</title><author>Fang, Yan ; Zeng, Xu ; Yan, Peng ; Jing, Zhenzi ; Jin, Fangming</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a388t-c4b6862185850fd08092f5b4984d0c60bf2ede812fd60fe0c9c392492137dadd3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2012</creationdate><topic>Acetic acid</topic><topic>Applied sciences</topic><topic>Carbohydrates</topic><topic>Catalysts</topic><topic>Chemical engineering</topic><topic>Exact sciences and technology</topic><topic>Fructose</topic><topic>Glucose</topic><topic>Industrial engineering</topic><topic>Purity</topic><topic>Reaction time</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Fang, Yan</creatorcontrib><creatorcontrib>Zeng, Xu</creatorcontrib><creatorcontrib>Yan, Peng</creatorcontrib><creatorcontrib>Jing, Zhenzi</creatorcontrib><creatorcontrib>Jin, Fangming</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Materials Research Database</collection><jtitle>Industrial & engineering chemistry research</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Fang, Yan</au><au>Zeng, Xu</au><au>Yan, Peng</au><au>Jing, Zhenzi</au><au>Jin, Fangming</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>An Acidic Two-Step Hydrothermal Process To Enhance Acetic Acid Production from Carbohydrate Biomass</atitle><jtitle>Industrial & engineering chemistry research</jtitle><addtitle>Ind. Eng. Chem. Res</addtitle><date>2012-03-28</date><risdate>2012</risdate><volume>51</volume><issue>12</issue><spage>4759</spage><epage>4763</epage><pages>4759-4763</pages><issn>0888-5885</issn><eissn>1520-5045</eissn><coden>IECRED</coden><abstract>An acidic two-step hydrothermal process to improve acetic acid production was investigated. In the first-step reaction, levulinic acid is formed in the presence of an acid catalyst. In the second-step reaction, the levulinic acid is converted into acetic acid via oxidation with newly supplied oxygen. The acetic acid yield from this two-step process was much higher than that without the acid catalysts in the first step. The acetic acid yield reached 23% with a purity of 47% from glucose and 26% with a purity of 52% from fructose. These yields were achieved at a reaction temperature of 523 K, a reaction time of 300 s, and pH 0.5 with HCl as an acid catalyst for the first step and at a reaction temperature of 523 K, a reaction time of 60 s, and an oxygen supply of 100% for the second step.</abstract><cop>Washington, DC</cop><pub>American Chemical Society</pub><doi>10.1021/ie202506c</doi><tpages>5</tpages></addata></record> |
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subjects | Acetic acid Applied sciences Carbohydrates Catalysts Chemical engineering Exact sciences and technology Fructose Glucose Industrial engineering Purity Reaction time |
title | An Acidic Two-Step Hydrothermal Process To Enhance Acetic Acid Production from Carbohydrate Biomass |
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