发明名称 Hydrogenation catalyst and use thereof for hydrogenating fischer-tropsch endproducts
摘要 A hydrogenation catalyst particularly suitable for hydrogenating oxygenates in a hydrogenation unit of a Fischer-Tropsch plant is disclosed. A preferred embodiment comprises more than 5% and less than 20% nickel based on a wide pore alumina support. The catalyst successfully hydrogenates oxygenates which otherwise tend to poison a catalyst in a hydroconversion unit downstream. Moreover, the temperature at which the unwanted hydrogenolysis of long chain paraffins to methane occurs is higher for one catalyst disclosed herein than a comparable known catalyst. This allows the hydrogenation plant to operate at a higher temperature.
申请公布号 US9333492(B2) 申请公布日期 2016.05.10
申请号 US200612161634 申请日期 2006.01.23
申请人 Shell Oil Company 发明人 Bijlsma Focco Cornelis;Dierickx Jan Lodewijk Maria;Hoek Arend;Kellendonk Frans Joris Antonius;Oud Anna Elisabeth Maria
分类号 B01J21/00;B01J23/00;B01J25/00;B01J29/00;B01J23/755;B01J21/04;B01J35/10;B01J37/02;C10G45/00;C10G3/00;C10G45/06;C10G45/12;C10G2/00 主分类号 B01J21/00
代理机构 代理人
主权项 1. A hydrogenation catalyst, the catalyst comprising a metallic active portion comprising nickel crystallites and a support comprising wide pore alumina, wherein the support does not catalyse an acid catalysed reaction and wherein over 90% of the pores within the support are sized between 100 Å-400 Å, wherein the catalyst comprises between 5 and 20% nickel and wherein the nickel crystallites are around 2.5 nm.
地址 Houston TX US