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Acetic acid production by selective oxidation of ethanol using Au catalysts supported on various metal oxide
The liquid-phase oxidation of ethanol to acetic acid using Au catalysts supported on various metal oxides was studied at 150°C using molecular oxygen as stoichiometric oxidant. Catalysts containing 1 wt% Au supported on TiO 2 , Al 2 O 3 , and ZnO were examined for ethanol oxidation. The results show...
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Published in: | Gold Bulletin 2009-01, Vol.42 (4), p.321-327 |
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creator | Tembe, Steton M. Patrick, Gary Scurrell, Mike S. |
description | The liquid-phase oxidation of ethanol to acetic acid using Au catalysts supported on various metal oxides was studied at 150°C using molecular oxygen as stoichiometric oxidant. Catalysts containing 1 wt% Au supported on TiO
2
, Al
2
O
3
, and ZnO were examined for ethanol oxidation. The results showed that ZnO and TiO
2
gave higher initial activities as supports for gold in ethanol oxidation, followed by Al
2
O
3
. Ethanol conversions of >90% and selectivities to acetic acid of >95% were achieved when using ZnO and TiO
2
as supports under conditions where a slight oxygen deficiency was used. With a slight excess of oxygen present initially, ethanol conversions of 99.4%, and a selectivity to acetic acid selectivity of 99.8% could be achieved. Gold leaching seemed to be very apparent with alumina as support and also, after continued use with titania-based catalysts. The use of higher initial concentrations of ethanol (range studied 5–40 mass% ethanol in water) led to higher ethyl acetate selectivities. High acetic acid selectivities were seen for relatively low (5–10 mass%) initial ethanol concentrations. |
doi_str_mv | 10.1007/BF03214954 |
format | article |
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2
, Al
2
O
3
, and ZnO were examined for ethanol oxidation. The results showed that ZnO and TiO
2
gave higher initial activities as supports for gold in ethanol oxidation, followed by Al
2
O
3
. Ethanol conversions of >90% and selectivities to acetic acid of >95% were achieved when using ZnO and TiO
2
as supports under conditions where a slight oxygen deficiency was used. With a slight excess of oxygen present initially, ethanol conversions of 99.4%, and a selectivity to acetic acid selectivity of 99.8% could be achieved. Gold leaching seemed to be very apparent with alumina as support and also, after continued use with titania-based catalysts. The use of higher initial concentrations of ethanol (range studied 5–40 mass% ethanol in water) led to higher ethyl acetate selectivities. High acetic acid selectivities were seen for relatively low (5–10 mass%) initial ethanol concentrations.</description><identifier>ISSN: 0017-1557</identifier><identifier>EISSN: 2190-7579</identifier><identifier>DOI: 10.1007/BF03214954</identifier><language>eng</language><publisher>Berlin/Heidelberg: Springer-Verlag</publisher><subject>Chemistry and Materials Science ; Materials Science ; Metallic Materials</subject><ispartof>Gold Bulletin, 2009-01, Vol.42 (4), p.321-327</ispartof><rights>World Gold Council 2009</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c369t-31ef88e3626cb7caf2fadc51f437404b885a4eac0be5a57e1b169b589f54c9923</citedby><cites>FETCH-LOGICAL-c369t-31ef88e3626cb7caf2fadc51f437404b885a4eac0be5a57e1b169b589f54c9923</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids></links><search><creatorcontrib>Tembe, Steton M.</creatorcontrib><creatorcontrib>Patrick, Gary</creatorcontrib><creatorcontrib>Scurrell, Mike S.</creatorcontrib><title>Acetic acid production by selective oxidation of ethanol using Au catalysts supported on various metal oxide</title><title>Gold Bulletin</title><addtitle>Gold Bull</addtitle><description>The liquid-phase oxidation of ethanol to acetic acid using Au catalysts supported on various metal oxides was studied at 150°C using molecular oxygen as stoichiometric oxidant. Catalysts containing 1 wt% Au supported on TiO
2
, Al
2
O
3
, and ZnO were examined for ethanol oxidation. The results showed that ZnO and TiO
2
gave higher initial activities as supports for gold in ethanol oxidation, followed by Al
2
O
3
. Ethanol conversions of >90% and selectivities to acetic acid of >95% were achieved when using ZnO and TiO
2
as supports under conditions where a slight oxygen deficiency was used. With a slight excess of oxygen present initially, ethanol conversions of 99.4%, and a selectivity to acetic acid selectivity of 99.8% could be achieved. Gold leaching seemed to be very apparent with alumina as support and also, after continued use with titania-based catalysts. The use of higher initial concentrations of ethanol (range studied 5–40 mass% ethanol in water) led to higher ethyl acetate selectivities. High acetic acid selectivities were seen for relatively low (5–10 mass%) initial ethanol concentrations.</description><subject>Chemistry and Materials Science</subject><subject>Materials Science</subject><subject>Metallic Materials</subject><issn>0017-1557</issn><issn>2190-7579</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2009</creationdate><recordtype>article</recordtype><recordid>eNptkEFLAzEQhYMoWGov_oKcldVkk2w2x1qsCgUvel6y2UlN2W6WJFvsvzdawYtzeczMx-PxELqm5I4SIu8f1oSVlCvBz9CspIoUUkh1jmaEUFlQIeQlWsS4I3kUp4xWM9QvDSRnsDauw2Pw3WSS8wNujzhCD3k5APafrtM_Z28xpA89-B5P0Q1bvJyw0Un3x5gijtM4-pCgwxk96OD8FPEe8vvHAq7QhdV9hMWvztH7-vFt9VxsXp9eVstNYVilUsEo2LoGVpWVaaXRtrS6M4JaziQnvK1roTloQ1oQWkigLa1UK2plBTdKlWyObk6-JvgYA9hmDG6vw7GhpPmuqvmrKsO3JzhmaNhCaHZ-CkPO9x_9BQ0MaxQ</recordid><startdate>20090101</startdate><enddate>20090101</enddate><creator>Tembe, Steton M.</creator><creator>Patrick, Gary</creator><creator>Scurrell, Mike S.</creator><general>Springer-Verlag</general><scope>C6C</scope><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20090101</creationdate><title>Acetic acid production by selective oxidation of ethanol using Au catalysts supported on various metal oxide</title><author>Tembe, Steton M. ; Patrick, Gary ; Scurrell, Mike S.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c369t-31ef88e3626cb7caf2fadc51f437404b885a4eac0be5a57e1b169b589f54c9923</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2009</creationdate><topic>Chemistry and Materials Science</topic><topic>Materials Science</topic><topic>Metallic Materials</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Tembe, Steton M.</creatorcontrib><creatorcontrib>Patrick, Gary</creatorcontrib><creatorcontrib>Scurrell, Mike S.</creatorcontrib><collection>SpringerOpen</collection><collection>CrossRef</collection><jtitle>Gold Bulletin</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Tembe, Steton M.</au><au>Patrick, Gary</au><au>Scurrell, Mike S.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Acetic acid production by selective oxidation of ethanol using Au catalysts supported on various metal oxide</atitle><jtitle>Gold Bulletin</jtitle><stitle>Gold Bull</stitle><date>2009-01-01</date><risdate>2009</risdate><volume>42</volume><issue>4</issue><spage>321</spage><epage>327</epage><pages>321-327</pages><issn>0017-1557</issn><eissn>2190-7579</eissn><abstract>The liquid-phase oxidation of ethanol to acetic acid using Au catalysts supported on various metal oxides was studied at 150°C using molecular oxygen as stoichiometric oxidant. Catalysts containing 1 wt% Au supported on TiO
2
, Al
2
O
3
, and ZnO were examined for ethanol oxidation. The results showed that ZnO and TiO
2
gave higher initial activities as supports for gold in ethanol oxidation, followed by Al
2
O
3
. Ethanol conversions of >90% and selectivities to acetic acid of >95% were achieved when using ZnO and TiO
2
as supports under conditions where a slight oxygen deficiency was used. With a slight excess of oxygen present initially, ethanol conversions of 99.4%, and a selectivity to acetic acid selectivity of 99.8% could be achieved. Gold leaching seemed to be very apparent with alumina as support and also, after continued use with titania-based catalysts. The use of higher initial concentrations of ethanol (range studied 5–40 mass% ethanol in water) led to higher ethyl acetate selectivities. High acetic acid selectivities were seen for relatively low (5–10 mass%) initial ethanol concentrations.</abstract><cop>Berlin/Heidelberg</cop><pub>Springer-Verlag</pub><doi>10.1007/BF03214954</doi><tpages>7</tpages><oa>free_for_read</oa></addata></record> |
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language | eng |
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source | Springer Nature |
subjects | Chemistry and Materials Science Materials Science Metallic Materials |
title | Acetic acid production by selective oxidation of ethanol using Au catalysts supported on various metal oxide |
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