Selective Hydrogenation Catalyst and Methods of Making and Using Same
申请人:Cheung Tin-Tack Peter
公开号:US20100228065A1
公开(公告)日:2010-09-09
A composition comprising a supported hydrogenation catalyst comprising palladium and an organophosphorous compound, the supported hydrogenation catalyst being capable of selectively hydrogenating highly unsaturated hydrocarbons to unsaturated hydrocarbons. A method of making a selective hydrogenation catalyst comprising contacting a support with a palladium-containing compound to form a palladium supported composition, contacting the palladium supported composition with an organophosphorus compound to form a catalyst precursor, and reducing the catalyst precursor to form the catalyst. A method of selectively hydrogenating highly unsaturated hydrocarbons to an unsaturated hydrocarbon enriched composition comprising contacting a supported catalyst comprising palladium and an organophosphorous compound with a feed comprising highly unsaturated hydrocarbon under conditions suitable for hydrogenating at least a portion of the highly unsaturated hydrocarbon feed to form the unsaturated hydrocarbon enriched composition.
SELECTIVE HYDROGENATION CATALYST AND METHODS OF MAKING AND USING SAME
申请人:Chevron Phillips Chemical Company LP
公开号:EP3144064A2
公开(公告)日:2017-03-22
A composition comprising a supported hydrogenation catalyst comprising palladium and an organophosphorous compound, the supported hydrogenation catalyst being capable of selectively hydrogenating highly unsaturated hydrocarbons to unsaturated hydrocarbons.
SELECTIVE HYDROGENATION CATALYST AND METHODS OF MAKING AND USING SAME
申请人:Chevron Phillips Chemical Company LP
公开号:EP2403642A2
公开(公告)日:2012-01-11
METHODS OF USING A SELECTIVE HYDROGENATION CATALYST
申请人:Chevron Phillips Chemical Company LP
公开号:EP2403642B1
公开(公告)日:2017-08-02
Hydrogenation Using Highly Selective Catalyst
申请人:Chevron Phillips Chemical Company LP
公开号:US20160355449A1
公开(公告)日:2016-12-08
A process comprising hydrogenating a highly unsaturated hydrocarbon in the presence of a first hydrogenation catalyst and a second hydrogenation catalyst to one or more compounds including an unsaturated hydrocarbon such that a total conversion of the highly unsaturated hydrocarbon is about 99 mol % or greater. In the process, the first hydrogenation catalyst, the second hydrogenation catalyst, or both, have a hydrogenation selectivity to the unsaturated hydrocarbon of about 90% or greater.