发明名称 Catalyst for the hydrogenation of unsaturated hydrocarbons and process for its preparation
摘要 The present invention relates to a catalyst for the hydrogenation of unsaturated hydrocarbons, in particular aromatics with a broad molecular weight range, a process for the production thereof and a process for hydrogenating unsaturated hydrocarbons.
申请公布号 US8841498(B2) 申请公布日期 2014.09.23
申请号 US201313944968 申请日期 2013.07.18
申请人 Shell Oil Company 发明人 Birke Peter;Geyer Reinhard;Hunold Jurgen;Kraak Peter;Schoedel Rainer
分类号 C07C5/10;B01J21/00;C10G45/00;B01J23/755;C10G45/08;B01J37/03;C10G45/48;B01J23/78;B01J23/86;B01J23/80;B01J35/10;B01J37/18;B01J37/00;B01J35/00;B01J37/14;B01J21/08 主分类号 C07C5/10
代理机构 代理人
主权项 1. A process for the preparation of a supported nickel on silica catalyst which catalyst has a nickel content of 40 to 85 weight-% (calculated as NiO), a silicon content of 15 to 60 weight-% (calculated as SiO2), a titanium content of 0.5 to 5.0 weight-% (calculated as TiO2), and does not contain more than 0.20 weight-% iron (calculated as Fe), wherein the catalyst has a monomodal Ni-crystallite size distribution with a mean crystallite size of the reduced catalyst of 1.5 to 3.5 nm, a pore volume of at least 0.60 ml/g and wherein the proportion of the pore volume of pores with a pore diameter of ≧10 nm is at least 55%; wherein the process comprises reacting a metal salt solution which comprises a nickel ion source and a titanium ion source and which is substantially free of iron with a sodium waterglass solution, which waterglass is a SiO2 source, at a pH from 8 to 9.5 and at a temperature from 70° C. to 100° C., so as to co-precipitate a catalyst material and recovering the co-precipitated catalyst material to obtain a supported nickel on silica catalyst, and optionally drying, calcining and reducing.
地址 Houston TX US