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 |