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Selective Vapor-Phase Hydrogenation of Furfural to Furfuryl Alcohol over Cu/Silica Catalysts
Vapor-phase hydrogenation of furfural (FAL) to furfuryl alcohol (FOL) was performed over 20 wt.% Cu supported on SiO2 under H2 pressure. The Cu/SiO2 catalyst with a pore size of 6 nm or larger provided FOL selectivity higher than 99% even at a high FAL conversion, whereas hydrogenolysis of FOL to 2-...
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Published in: | Bulletin of the Chemical Society of Japan 2023-01, Vol.96 (1), p.8-15 |
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creator | Kurniawan, Enggah Hayashi, Tetsugaku Hosaka, Shuya Yamada, Yasuhiro Sato, Satoshi |
description | Vapor-phase hydrogenation of furfural (FAL) to furfuryl alcohol (FOL) was performed over 20 wt.% Cu supported on SiO2 under H2 pressure. The Cu/SiO2 catalyst with a pore size of 6 nm or larger provided FOL selectivity higher than 99% even at a high FAL conversion, whereas hydrogenolysis of FOL to 2-methylfuran (MF) proceeded over the Cu/SiO2 catalyst with small mesopores of 3 nm even at low FAL conversion. The selective transformation of FAL to FOL was regulated by the reaction temperature, H2 pressure, and contact time: the high FOL selectivity was achieved by minimizing the stepwise hydrogenolysis of FOL to MF, which is favorable under severe conditions. Under the optimum conditions, the FOL productivity was 3.1 kgFOL kgcat−1 h−1 with a FOL selectivity above 99% at 150 °C and an H2 pressure of 2.0 MPa. Furthermore, the Cu/SiO2 catalyst could maintain the high activity on stream for 5 h, with no significant catalyst deactivation. |
doi_str_mv | 10.1246/bcsj.20220285 |
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The Cu/SiO2 catalyst with a pore size of 6 nm or larger provided FOL selectivity higher than 99% even at a high FAL conversion, whereas hydrogenolysis of FOL to 2-methylfuran (MF) proceeded over the Cu/SiO2 catalyst with small mesopores of 3 nm even at low FAL conversion. The selective transformation of FAL to FOL was regulated by the reaction temperature, H2 pressure, and contact time: the high FOL selectivity was achieved by minimizing the stepwise hydrogenolysis of FOL to MF, which is favorable under severe conditions. Under the optimum conditions, the FOL productivity was 3.1 kgFOL kgcat−1 h−1 with a FOL selectivity above 99% at 150 °C and an H2 pressure of 2.0 MPa. 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Furthermore, the Cu/SiO2 catalyst could maintain the high activity on stream for 5 h, with no significant catalyst deactivation.</description><subject>Catalysts</subject><subject>Contact pressure</subject><subject>Conversion</subject><subject>Furfural</subject><subject>Furfuryl alcohol</subject><subject>Hydrogenation</subject><subject>Hydrogenolysis</subject><subject>Pore size</subject><subject>Selectivity</subject><subject>Silicon dioxide</subject><issn>0009-2673</issn><issn>1348-0634</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2023</creationdate><recordtype>article</recordtype><recordid>eNptkM1Lw0AQxRdRsFaP3hc8p93vbLyVoFYoKFQ9CWGz3diEbTbubgr5701pxYsw8GbgN_OYB8AtRjNMmJiXOjQzgshYkp-BCaZMJkhQdg4mCKEsISKll-AqhGYcJWfZBHyujTU61nsDP1TnfPK6VcHA5bDx7su0Ktauha6Cj72veq8sjO7UDxYurHZbZ6HbGw_zfr6uba0VzFVUdggxXIOLStlgbk46Be-PD2_5Mlm9PD3ni1WiqSQxwTxDGStJSSXFG0G1KDVBiHOtNCNcojJLOcVcmEplMmWj6EqYMsM4NbSSdArujnc77757E2LRuN63o2VBUilSzGjKRio5Utq7ELypis7XO-WHAqPiEGBxCLD4DXDk70_81uzGv2xwujZxaFSn2j-H_5d_AKWxd84</recordid><startdate>20230101</startdate><enddate>20230101</enddate><creator>Kurniawan, Enggah</creator><creator>Hayashi, Tetsugaku</creator><creator>Hosaka, Shuya</creator><creator>Yamada, Yasuhiro</creator><creator>Sato, Satoshi</creator><general>The Chemical Society of Japan</general><general>Chemical Society of Japan</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>8BQ</scope><scope>8FD</scope><scope>JG9</scope></search><sort><creationdate>20230101</creationdate><title>Selective Vapor-Phase Hydrogenation of Furfural to Furfuryl Alcohol over Cu/Silica Catalysts</title><author>Kurniawan, Enggah ; Hayashi, Tetsugaku ; Hosaka, Shuya ; Yamada, Yasuhiro ; Sato, Satoshi</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c382t-159094b2b3831d63c6bc20055cac42580b9753156efa9874efacf6eb9117e3f83</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2023</creationdate><topic>Catalysts</topic><topic>Contact pressure</topic><topic>Conversion</topic><topic>Furfural</topic><topic>Furfuryl alcohol</topic><topic>Hydrogenation</topic><topic>Hydrogenolysis</topic><topic>Pore size</topic><topic>Selectivity</topic><topic>Silicon dioxide</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Kurniawan, Enggah</creatorcontrib><creatorcontrib>Hayashi, Tetsugaku</creatorcontrib><creatorcontrib>Hosaka, Shuya</creatorcontrib><creatorcontrib>Yamada, Yasuhiro</creatorcontrib><creatorcontrib>Sato, Satoshi</creatorcontrib><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><jtitle>Bulletin of the Chemical Society of Japan</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Kurniawan, Enggah</au><au>Hayashi, Tetsugaku</au><au>Hosaka, Shuya</au><au>Yamada, Yasuhiro</au><au>Sato, Satoshi</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Selective Vapor-Phase Hydrogenation of Furfural to Furfuryl Alcohol over Cu/Silica Catalysts</atitle><jtitle>Bulletin of the Chemical Society of Japan</jtitle><date>2023-01-01</date><risdate>2023</risdate><volume>96</volume><issue>1</issue><spage>8</spage><epage>15</epage><pages>8-15</pages><issn>0009-2673</issn><eissn>1348-0634</eissn><abstract>Vapor-phase hydrogenation of furfural (FAL) to furfuryl alcohol (FOL) was performed over 20 wt.% Cu supported on SiO2 under H2 pressure. The Cu/SiO2 catalyst with a pore size of 6 nm or larger provided FOL selectivity higher than 99% even at a high FAL conversion, whereas hydrogenolysis of FOL to 2-methylfuran (MF) proceeded over the Cu/SiO2 catalyst with small mesopores of 3 nm even at low FAL conversion. The selective transformation of FAL to FOL was regulated by the reaction temperature, H2 pressure, and contact time: the high FOL selectivity was achieved by minimizing the stepwise hydrogenolysis of FOL to MF, which is favorable under severe conditions. Under the optimum conditions, the FOL productivity was 3.1 kgFOL kgcat−1 h−1 with a FOL selectivity above 99% at 150 °C and an H2 pressure of 2.0 MPa. Furthermore, the Cu/SiO2 catalyst could maintain the high activity on stream for 5 h, with no significant catalyst deactivation.</abstract><cop>Tokyo</cop><pub>The Chemical Society of Japan</pub><doi>10.1246/bcsj.20220285</doi><tpages>8</tpages><oa>free_for_read</oa></addata></record> |
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source | Oxford Journals Online |
subjects | Catalysts Contact pressure Conversion Furfural Furfuryl alcohol Hydrogenation Hydrogenolysis Pore size Selectivity Silicon dioxide |
title | Selective Vapor-Phase Hydrogenation of Furfural to Furfuryl Alcohol over Cu/Silica Catalysts |
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