DIRECT AND SELECTIVE PRODUCTION OF ETHYL ACETATE FROM ACETIC ACID UTILIZING A BIMETAL SUPPORTED CATALYST
Disclosed is a process for selective and direct formation of ethyl acetate from acetic acid comprising: contacting a feed stream containing acetic acid and hydrogen in the vapour phase at a temperature in the range of 200°C to 300°C with a hydrogenating catalyst containing platinum or palladium and...
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creator | VAN DER WAAL, JAN CORNELIS ZUZANIUK, VIRGINIE REPMAN, DEBORAH R CHAPMAN, JOSEFINA T ZINK, JAMES H CHEN, LAIYUAN JOHNSTON, VICTOR J KIMMICH, BARBARA F |
description | Disclosed is a process for selective and direct formation of ethyl acetate from acetic acid comprising: contacting a feed stream containing acetic acid and hydrogen in the vapour phase at a temperature in the range of 200°C to 300°C with a hydrogenating catalyst containing platinum or palladium and copper or cobalt on a catalyst support, where the weight ratio of platinum or palladium to copper or cobalt is in the range of 0.1 to 1. Also disclosed is a process for selective and direct formation of ethyl acetate from acetic acid using a hydrogenating catalyst selected from nickel/molybdenum (Ni/Mo), palladium/ molybdenum (Pd/Mo), or platinum/molybdenum (Pt/Mo) supported on H-ZSM-5. |
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Also disclosed is a process for selective and direct formation of ethyl acetate from acetic acid using a hydrogenating catalyst selected from nickel/molybdenum (Ni/Mo), palladium/ molybdenum (Pd/Mo), or platinum/molybdenum (Pt/Mo) supported on H-ZSM-5.</description><language>eng</language><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS ; CHEMISTRY ; METALLURGY ; ORGANIC CHEMISTRY</subject><creationdate>2012</creationdate><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20120727&DB=EPODOC&CC=NZ&NR=591041A$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,777,882,25545,76296</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20120727&DB=EPODOC&CC=NZ&NR=591041A$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>VAN DER WAAL, JAN CORNELIS</creatorcontrib><creatorcontrib>ZUZANIUK, VIRGINIE</creatorcontrib><creatorcontrib>REPMAN, DEBORAH R</creatorcontrib><creatorcontrib>CHAPMAN, JOSEFINA T</creatorcontrib><creatorcontrib>ZINK, JAMES H</creatorcontrib><creatorcontrib>CHEN, LAIYUAN</creatorcontrib><creatorcontrib>JOHNSTON, VICTOR J</creatorcontrib><creatorcontrib>KIMMICH, BARBARA F</creatorcontrib><title>DIRECT AND SELECTIVE PRODUCTION OF ETHYL ACETATE FROM ACETIC ACID UTILIZING A BIMETAL SUPPORTED CATALYST</title><description>Disclosed is a process for selective and direct formation of ethyl acetate from acetic acid comprising: contacting a feed stream containing acetic acid and hydrogen in the vapour phase at a temperature in the range of 200°C to 300°C with a hydrogenating catalyst containing platinum or palladium and copper or cobalt on a catalyst support, where the weight ratio of platinum or palladium to copper or cobalt is in the range of 0.1 to 1. 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Also disclosed is a process for selective and direct formation of ethyl acetate from acetic acid using a hydrogenating catalyst selected from nickel/molybdenum (Ni/Mo), palladium/ molybdenum (Pd/Mo), or platinum/molybdenum (Pt/Mo) supported on H-ZSM-5.</abstract><oa>free_for_read</oa></addata></record> |
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subjects | ACYCLIC OR CARBOCYCLIC COMPOUNDS CHEMISTRY METALLURGY ORGANIC CHEMISTRY |
title | DIRECT AND SELECTIVE PRODUCTION OF ETHYL ACETATE FROM ACETIC ACID UTILIZING A BIMETAL SUPPORTED CATALYST |
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