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Demetallisation of residual oils - with metal-silica catalysts with specified pore characteristics and a low loss on ignition

机译:残留油的脱金属-使用具有特定孔隙特征且燃烧损失低的金属-二氧化硅催化剂

摘要

The demetallisation of residual oils before catalytic conversion is carried out by contacting the oil at high temp. and pressure, in the presence of H2, with a catalyst comprising one or more metals with hydrogenating activity on a support, the catalyst satisfying the following requirements: (1) p/d 3.5-0.02v, where p is the specific av. pore dia. (nm), d is the specific av. particle dia. (mm), and v is the percentage of the total pore vol. in pores with a dia. of 100 nm; (2) the total pore vol. is =0.40 ml/g; (3) v 50; (4) the specific surface is 100 m2; (5) when 3.5-0.02 p/d =10-0.15v, the N2 pore vol. is 0.60 ml/g, the specific surface is 150 m2/g and p 5 nm; (6) the catalyst contains 0.1-15 pts. wt. of the hydrogenating metals per 100 pts wt. of SiO2 support; (7) the loss on ignition of the catalyst is 1.0 wt. % (0.5 wt. % when vanadium is one of the hydrogenating metals). When condition (7) is met, catalysts satisfying requirements (1)-(6) have optimum activity. Catalysts satisfying requirement (1)-(5) are described in the parent patent.
机译:残余油的脱金属在催化转化之前是通过使油在高温下进行的。在H 2存在下,用包含在载体上具有氢化活性的一种或多种金属的催化剂,在压力和压力下,该催化剂满足以下要求:(1)p / d> 3.5-0.02v,其中p是比值av。孔直径(nm),d是比值av。颗粒直径(mm),v是总孔隙体积的百分比。在毛孔直径上。 > 100 nm; (2)总孔体积。 > = 0.40毫升/克; (3)第50节; (4)比表面积> 100 m2; (5)当3.5-0.02 p / d = 10-0.15v时,N2孔体积> 0.60 ml / g,比表面积> 150 m2 / g,p> 5 nm; (6)催化剂含0.1-15 pts。重量每100 pts重量的氢化金属数量SiO2载体(7)催化剂的燃烧损失为1.0重量%。 %(当钒是氢化金属之一时为0.5%)。当满足条件(7)时,满足要求(1)-(6)的催化剂具有最佳活性。在母专利中描述了满足要求(1)-(5)的催化剂。

著录项

  • 公开/公告号NL7410162A

    专利类型

  • 公开/公告日1976-02-02

    原文格式PDF

  • 申请/专利号NL19740010162

  • 发明设计人

    申请日1974-07-29

  • 分类号B01J23/84;B01J35/10;C10G23/02;C10G37/06;

  • 国家 NL

  • 入库时间 2022-08-23 02:51:07

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