Efficient Synthesis of Furfuryl Alcohol and 2‐Methylfuran from Furfural over Mineral‐Derived Cu/ZnO Catalysts

Two kinds of typical mineral‐derived Cu/ZnO catalysts consisting of aurichalcite and zincian malachite were introduced for furfural hydrogenation to furfuryl alcohol (FOL) and 2‐methylfuran (2‐MF) in a fixed‐bed reactor. Under proper reaction conditions, high yields of FOL (above 99 %) and 2‐MF (94....

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Veröffentlicht in:ChemCatChem 2017-08, Vol.9 (15), p.3023-3030
Hauptverfasser: Yang, Xiaohai, Xiang, Xiaomin, Chen, Hongmei, Zheng, Hongyan, Li, Yong‐Wang, Zhu, Yulei
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container_issue 15
container_start_page 3023
container_title ChemCatChem
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creator Yang, Xiaohai
Xiang, Xiaomin
Chen, Hongmei
Zheng, Hongyan
Li, Yong‐Wang
Zhu, Yulei
description Two kinds of typical mineral‐derived Cu/ZnO catalysts consisting of aurichalcite and zincian malachite were introduced for furfural hydrogenation to furfuryl alcohol (FOL) and 2‐methylfuran (2‐MF) in a fixed‐bed reactor. Under proper reaction conditions, high yields of FOL (above 99 %) and 2‐MF (94.5 %) could be obtained over the aurichalcite Cu/ZnO catalyst (AC‐CZ), whereas the best yield of 2‐MF was only 76.9 % (0.5 h−1) over the zincian malachite Cu/ZnO catalyst (ZM‐CZ). The normalized productivity of 2‐MF was 43.5 mol kgCu−1 h−1 and 17.4 mol kgCu−1 h−1 for AC‐CZ and ZM‐CZ, respectively (LHSV=1.5 h−1). The catalysts were characterized by XRD analysis, Raman spectra, CO IR spectroscopy, H2 temperature‐programmed reduction, N2O titration, NH3 temperature‐programmed desorption, and X‐ray photoelectron spectroscopy. The far better performance of AC‐CZ in furfural hydrogenation was ascribed to its higher dispersion of copper species, superior copper surface area, better surface acidity distribution, and stronger Cu0–ZnO synergy. In addition, the surface acidity of the catalysts seemed to have a higher influence on 2‐MF production than the Cu surface area, but the optimal balance of both factors still needs to be investigated systematically. The cheaper, the better: A Cu/ZnO catalyst derived from aurichalcite having a lower copper cost shows far better performance in the furfural hydrogenation to furfuryl alcohol and 2‐methylfuran than that derived from zincian malachite.
doi_str_mv 10.1002/cctc.201700279
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Under proper reaction conditions, high yields of FOL (above 99 %) and 2‐MF (94.5 %) could be obtained over the aurichalcite Cu/ZnO catalyst (AC‐CZ), whereas the best yield of 2‐MF was only 76.9 % (0.5 h−1) over the zincian malachite Cu/ZnO catalyst (ZM‐CZ). The normalized productivity of 2‐MF was 43.5 mol kgCu−1 h−1 and 17.4 mol kgCu−1 h−1 for AC‐CZ and ZM‐CZ, respectively (LHSV=1.5 h−1). The catalysts were characterized by XRD analysis, Raman spectra, CO IR spectroscopy, H2 temperature‐programmed reduction, N2O titration, NH3 temperature‐programmed desorption, and X‐ray photoelectron spectroscopy. The far better performance of AC‐CZ in furfural hydrogenation was ascribed to its higher dispersion of copper species, superior copper surface area, better surface acidity distribution, and stronger Cu0–ZnO synergy. In addition, the surface acidity of the catalysts seemed to have a higher influence on 2‐MF production than the Cu surface area, but the optimal balance of both factors still needs to be investigated systematically. The cheaper, the better: A Cu/ZnO catalyst derived from aurichalcite having a lower copper cost shows far better performance in the furfural hydrogenation to furfuryl alcohol and 2‐methylfuran than that derived from zincian malachite.</description><identifier>ISSN: 1867-3880</identifier><identifier>EISSN: 1867-3899</identifier><identifier>DOI: 10.1002/cctc.201700279</identifier><language>eng</language><publisher>Weinheim: Wiley Subscription Services, Inc</publisher><subject>Alcohol ; aldehydes ; biomass ; Catalysts ; Copper ; Furfural ; Furfuryl alcohol ; Hydrogenation ; Infrared radiation ; Infrared spectroscopy ; Nitrous oxide ; Photoelectron spectroscopy ; Raman spectra ; Spectroscopic analysis ; Spectrum analysis ; Surface area ; Titration ; X-ray diffraction ; zinc ; Zinc oxide</subject><ispartof>ChemCatChem, 2017-08, Vol.9 (15), p.3023-3030</ispartof><rights>2017 Wiley‐VCH Verlag GmbH &amp; Co. KGaA, Weinheim</rights><rights>2017 Wiley-VCH Verlag GmbH &amp; Co. 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Under proper reaction conditions, high yields of FOL (above 99 %) and 2‐MF (94.5 %) could be obtained over the aurichalcite Cu/ZnO catalyst (AC‐CZ), whereas the best yield of 2‐MF was only 76.9 % (0.5 h−1) over the zincian malachite Cu/ZnO catalyst (ZM‐CZ). The normalized productivity of 2‐MF was 43.5 mol kgCu−1 h−1 and 17.4 mol kgCu−1 h−1 for AC‐CZ and ZM‐CZ, respectively (LHSV=1.5 h−1). The catalysts were characterized by XRD analysis, Raman spectra, CO IR spectroscopy, H2 temperature‐programmed reduction, N2O titration, NH3 temperature‐programmed desorption, and X‐ray photoelectron spectroscopy. The far better performance of AC‐CZ in furfural hydrogenation was ascribed to its higher dispersion of copper species, superior copper surface area, better surface acidity distribution, and stronger Cu0–ZnO synergy. In addition, the surface acidity of the catalysts seemed to have a higher influence on 2‐MF production than the Cu surface area, but the optimal balance of both factors still needs to be investigated systematically. The cheaper, the better: A Cu/ZnO catalyst derived from aurichalcite having a lower copper cost shows far better performance in the furfural hydrogenation to furfuryl alcohol and 2‐methylfuran than that derived from zincian malachite.</description><subject>Alcohol</subject><subject>aldehydes</subject><subject>biomass</subject><subject>Catalysts</subject><subject>Copper</subject><subject>Furfural</subject><subject>Furfuryl alcohol</subject><subject>Hydrogenation</subject><subject>Infrared radiation</subject><subject>Infrared spectroscopy</subject><subject>Nitrous oxide</subject><subject>Photoelectron spectroscopy</subject><subject>Raman spectra</subject><subject>Spectroscopic analysis</subject><subject>Spectrum analysis</subject><subject>Surface area</subject><subject>Titration</subject><subject>X-ray diffraction</subject><subject>zinc</subject><subject>Zinc oxide</subject><issn>1867-3880</issn><issn>1867-3899</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2017</creationdate><recordtype>article</recordtype><recordid>eNqFkL1uwjAUha2qlUpp186WOgP-Sex4RCn9kUAMpUsXyzi2CDIx2AlVtj5Cn7FP0iAQHTvde-79zr3SAeAeoyFGiIy0rvWQIMw7wcUF6OGM8QHNhLg89xm6BjcxrhFigvK0B3YTa0tdmqqGb21Vr0wsI_QWPjXBNqF1cOy0X3kHVVVA8vP1PTP1qnXdTlXQBr85kcpBvzcBzsrKdKIDH00o96aAeTP6qOYwV7VybazjLbiyykVzd6p98P40WeQvg-n8-TUfTweaYi4GrDDcplZQxghhqTWpyNiSC1JwgylPCM4USlPMKFOmWCbdFHGTUCI4sxnXtA8ejne3we8aE2u59k2oupcSC8JxQhgWHTU8Ujr4GIOxchvKjQqtxEgeYpWHWOU51s4gjobP0pn2H1rm-SL_8_4CELp91A</recordid><startdate>20170809</startdate><enddate>20170809</enddate><creator>Yang, Xiaohai</creator><creator>Xiang, Xiaomin</creator><creator>Chen, Hongmei</creator><creator>Zheng, Hongyan</creator><creator>Li, Yong‐Wang</creator><creator>Zhu, Yulei</creator><general>Wiley Subscription Services, Inc</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20170809</creationdate><title>Efficient Synthesis of Furfuryl Alcohol and 2‐Methylfuran from Furfural over Mineral‐Derived Cu/ZnO Catalysts</title><author>Yang, Xiaohai ; Xiang, Xiaomin ; Chen, Hongmei ; Zheng, Hongyan ; Li, Yong‐Wang ; Zhu, Yulei</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c3179-6de7f5f93662265fe5986b792d7e1374218a0551636aedb47e107e432976f87c3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2017</creationdate><topic>Alcohol</topic><topic>aldehydes</topic><topic>biomass</topic><topic>Catalysts</topic><topic>Copper</topic><topic>Furfural</topic><topic>Furfuryl alcohol</topic><topic>Hydrogenation</topic><topic>Infrared radiation</topic><topic>Infrared spectroscopy</topic><topic>Nitrous oxide</topic><topic>Photoelectron spectroscopy</topic><topic>Raman spectra</topic><topic>Spectroscopic analysis</topic><topic>Spectrum analysis</topic><topic>Surface area</topic><topic>Titration</topic><topic>X-ray diffraction</topic><topic>zinc</topic><topic>Zinc oxide</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Yang, Xiaohai</creatorcontrib><creatorcontrib>Xiang, Xiaomin</creatorcontrib><creatorcontrib>Chen, Hongmei</creatorcontrib><creatorcontrib>Zheng, Hongyan</creatorcontrib><creatorcontrib>Li, Yong‐Wang</creatorcontrib><creatorcontrib>Zhu, Yulei</creatorcontrib><collection>CrossRef</collection><jtitle>ChemCatChem</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Yang, Xiaohai</au><au>Xiang, Xiaomin</au><au>Chen, Hongmei</au><au>Zheng, Hongyan</au><au>Li, Yong‐Wang</au><au>Zhu, Yulei</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Efficient Synthesis of Furfuryl Alcohol and 2‐Methylfuran from Furfural over Mineral‐Derived Cu/ZnO Catalysts</atitle><jtitle>ChemCatChem</jtitle><date>2017-08-09</date><risdate>2017</risdate><volume>9</volume><issue>15</issue><spage>3023</spage><epage>3030</epage><pages>3023-3030</pages><issn>1867-3880</issn><eissn>1867-3899</eissn><abstract>Two kinds of typical mineral‐derived Cu/ZnO catalysts consisting of aurichalcite and zincian malachite were introduced for furfural hydrogenation to furfuryl alcohol (FOL) and 2‐methylfuran (2‐MF) in a fixed‐bed reactor. Under proper reaction conditions, high yields of FOL (above 99 %) and 2‐MF (94.5 %) could be obtained over the aurichalcite Cu/ZnO catalyst (AC‐CZ), whereas the best yield of 2‐MF was only 76.9 % (0.5 h−1) over the zincian malachite Cu/ZnO catalyst (ZM‐CZ). The normalized productivity of 2‐MF was 43.5 mol kgCu−1 h−1 and 17.4 mol kgCu−1 h−1 for AC‐CZ and ZM‐CZ, respectively (LHSV=1.5 h−1). The catalysts were characterized by XRD analysis, Raman spectra, CO IR spectroscopy, H2 temperature‐programmed reduction, N2O titration, NH3 temperature‐programmed desorption, and X‐ray photoelectron spectroscopy. The far better performance of AC‐CZ in furfural hydrogenation was ascribed to its higher dispersion of copper species, superior copper surface area, better surface acidity distribution, and stronger Cu0–ZnO synergy. In addition, the surface acidity of the catalysts seemed to have a higher influence on 2‐MF production than the Cu surface area, but the optimal balance of both factors still needs to be investigated systematically. The cheaper, the better: A Cu/ZnO catalyst derived from aurichalcite having a lower copper cost shows far better performance in the furfural hydrogenation to furfuryl alcohol and 2‐methylfuran than that derived from zincian malachite.</abstract><cop>Weinheim</cop><pub>Wiley Subscription Services, Inc</pub><doi>10.1002/cctc.201700279</doi><tpages>8</tpages></addata></record>
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subjects Alcohol
aldehydes
biomass
Catalysts
Copper
Furfural
Furfuryl alcohol
Hydrogenation
Infrared radiation
Infrared spectroscopy
Nitrous oxide
Photoelectron spectroscopy
Raman spectra
Spectroscopic analysis
Spectrum analysis
Surface area
Titration
X-ray diffraction
zinc
Zinc oxide
title Efficient Synthesis of Furfuryl Alcohol and 2‐Methylfuran from Furfural over Mineral‐Derived Cu/ZnO Catalysts
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