首页> 外国专利> process for the production of catalysts, the ausnickel and / or kobaltsulfid and molybdenum and / or on a porous carrier material wolframsulfid exist, and their use in the conversion of hydrocarbons

process for the production of catalysts, the ausnickel and / or kobaltsulfid and molybdenum and / or on a porous carrier material wolframsulfid exist, and their use in the conversion of hydrocarbons

机译:在生产催化剂的过程中,存在着奥氏体镍和/或钴硫化物和钼和/或在多孔载体材料上的硫丹,并且它们在烃类转化中的用途

摘要

1401620 Hydrocarbon conversion catalysts SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ NV 15 Aug 1972 [17 Aug 1971] 38525/71 Heading B1E [Also in Division C5] Catalysts comprising a sulphide of Ni, Co, Mo and/or W are made by treating a composition comprising a porous carrier, a watersoluble salt of Ni, Co, Mo and/or W and water with a hydrogen sulphide-containing gas at a temperature below 150‹C and subsequently heating up the material in a hydrogencontaining gas to a final temperature above 200‹C. The amount of water in the composition to be treated with the hydrogen sulphidecontaining gas corresponds to the amount present in the composition after drying in a dry gas at 110‹C + 20-120% of the amount which the dried composition can absorb in the pores of the carrier at 20‹C. The composition to be sulphided may be prepared by impregnation in one or more steps either with drying after each step, the drying after the last step being controlled to give the correct water content, or when each impregnation uses a volume of solution substantially equal to the pore volume of the carrier with drying after each step except the last. The hydrogen sulphide - containing gas may be pure H 2 S or H 2 S+H 2 and the hydrogen-containing gas may be H 2 S+H 2 .
机译:1401620烃转化催化剂SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ NV 1972年8月15日[1971年8月17日]标题B1E [Also在C5区]包含Ni,Co,Mo和/或W硫化物的催化剂是通过处理包含多孔载体,Ni,Co,Mo和/或W的水溶性盐和水与含硫化氢的气体的温度低于150°C,随后将材料在含氢的气体中加热至最终温度高于200°C 。待用含硫化氢的气体处理的组合物中的水量对应于在110°C的干燥气体中干燥后,组合物中存在的水量+干燥后的组合物在孔中可吸收的量的20-120%载体在20℃的温度。待硫化的组合物可通过在一个或多个步骤中浸渍而制备,或者在每个步骤之后进行干燥,控制最后一步之后的干燥以给出正确的水含量,或者在每次浸渍时使用的溶液的体积基本上等于水的体积。除最后一步外,每步干燥后的载体孔隙体积。含硫化氢的气体可以是纯H 2 S或H 2 S + H 2,而含氢的气体可以是H 2 S + H 2。

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