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WO2008060992A3 - Procédés d'hydrogénation sélective utilisant une composition catalytique de surface fonctionnelle - Google Patents

Procédés d'hydrogénation sélective utilisant une composition catalytique de surface fonctionnelle Download PDF

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Publication number
WO2008060992A3
WO2008060992A3 PCT/US2007/084231 US2007084231W WO2008060992A3 WO 2008060992 A3 WO2008060992 A3 WO 2008060992A3 US 2007084231 W US2007084231 W US 2007084231W WO 2008060992 A3 WO2008060992 A3 WO 2008060992A3
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Prior art keywords
equal
less
substrate
catalyst composition
selective hydrogenation
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PCT/US2007/084231
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WO2008060992A2 (fr
Inventor
Robert L Bedard
Jeffery C Bricker
Ally S Chan
Dean E Rende
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Uop Llc
Robert L Bedard
Jeffery C Bricker
Ally S Chan
Dean E Rende
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Application filed by Uop Llc, Robert L Bedard, Jeffery C Bricker, Ally S Chan, Dean E Rende filed Critical Uop Llc
Publication of WO2008060992A2 publication Critical patent/WO2008060992A2/fr
Publication of WO2008060992A3 publication Critical patent/WO2008060992A3/fr

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    • B01J21/06Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
    • B01J21/08Silica
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    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/32Selective hydrogenation of the diolefin or acetylene compounds
    • C10G45/34Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used
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Abstract

L'invention concerne des procédés d'hydrogénation sélective dans lesquels est utilisée une composition catalytique, qui comprend de préférence un substrat de verre; un ou plusieurs composants tensioactifs fonctionnels étant intégrés sur et/ou dans la surface du substrat. Un substrat sensiblement non microporeux/non mésoporeux qui comprend des macropores présente (i) une surface totale comprise entre 0,1 m2/g et 50 m2/g; et (ii) un point isoélectrique prédéterminé (IEP) obtenu dans une plage de pH supérieure à 0, de préférence supérieure ou égale à 4,5; ou idéalement supérieure ou égale à 6,0; mais inférieure ou égale à 14. Au moins une zone catalytiquement active peut être contiguë ou non contiguë et présente une épaisseur moyenne inférieure ou égale à environ 30 nm, de préférence inférieure ou égale à 20 nm et idéalement inférieure ou égale à 10 nm. De préférence, le substrat est une composition de verre présentant un SARCNa inférieur ou égal à environ 0,5.
PCT/US2007/084231 2006-11-11 2007-11-09 Procédés d'hydrogénation sélective utilisant une composition catalytique de surface fonctionnelle WO2008060992A2 (fr)

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JP5584906B2 (ja) * 2008-08-20 2014-09-10 ディーエスエム アイピー アセッツ ビー.ブイ. 多孔質シリカガラス上のパラジウムを含む新規の選択的水素化触媒およびその使用
TWI586693B (zh) 2013-07-23 2017-06-11 財團法人工業技術研究院 選擇性氫化共聚物的方法
RU2722157C1 (ru) 2015-07-22 2020-05-27 Басф Корпорейшн Катализаторы с высокой геометрической площадью поверхности для получения винилацетатного мономера

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EP0258942A2 (fr) * 1986-08-29 1988-03-09 Shell Internationale Researchmaatschappij B.V. Préparation de catalyseur
EP1044935A1 (fr) * 1999-04-13 2000-10-18 Ecole Polytechnique Federale De Lausanne Fibre de verre poreuse, résistante à poids léger ayant des propriétés physiques, chimiques ou biologiques
US20020035033A1 (en) * 1997-09-30 2002-03-21 Herbert Muller Process for preparing a shell-type catalyst

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EP0258942A2 (fr) * 1986-08-29 1988-03-09 Shell Internationale Researchmaatschappij B.V. Préparation de catalyseur
US20020035033A1 (en) * 1997-09-30 2002-03-21 Herbert Muller Process for preparing a shell-type catalyst
EP1044935A1 (fr) * 1999-04-13 2000-10-18 Ecole Polytechnique Federale De Lausanne Fibre de verre poreuse, résistante à poids léger ayant des propriétés physiques, chimiques ou biologiques

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