发明名称 Method for selective hydrogenation of phenylacetylene using composite bed in the presence of styrene
摘要 The present invention discloses a process for the selective hydrogenation of phenylacetylene in the presence of styrene conducted in a combined bed, which process comprises under hydrogenation reaction conditions, passing a hydrocarbon fraction feedstock containing phenylacetylene and styrene through a combined bed reactor containing a catalyst A and a catalyst B to contact the feedstock with the catalyst A and the catalyst B in turn, wherein the catalyst A is a nickel-based catalyst, the catalyst B is at least one selected from the group consisting of palladium-based catalysts and copper-based catalysts, and a weight ratio of the catalyst A loaded to the catalyst B loaded is from 0.5:1 to 5:1.
申请公布号 US8916736(B2) 申请公布日期 2014.12.23
申请号 US200913140645 申请日期 2009.12.17
申请人 Shanghai Research Institute of Petrochemical Technology, Sinopec;China Petroleum & Chemical Corporation 发明人 Li Siqin;Liu Juntao;Zhu Zhiyan;Zhu Junhua;Kuai Jun
分类号 C07C5/11;C07C7/167 主分类号 C07C5/11
代理机构 Finnegan, Henderson, Farabow, Garrett & Dunner LLP 代理人 Finnegan, Henderson, Farabow, Garrett & Dunner LLP
主权项 1. A process for the selective hydrogenation of phenylacetylene in the presence of styrene conducted in a combined bed, which process comprises under hydrogenation reaction conditions, passing a hydrocarbon fraction feedstock containing phenylacetylene and styrene through a combined bed reactor containing a catalyst A and a catalyst B, wherein the hydrocarbon fraction feedstock contacts with the catalyst A first and then the catalyst B, wherein the catalyst A is a nickel-based catalyst, the catalyst B is at least one selected from the group consisting of palladium-based catalysts and copper-based catalysts, and a weight ratio of the catalyst A loaded to the catalyst B loaded is from 0.5:1 to 5:1.
地址 Shanghai CN