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Method for depositing catalyst metals into zeolite to produce hydrocarbon processing catalyst

机译:将催化剂金属沉积到沸石中生产烃加工催化剂的方法

摘要

The present invention provides an ion exchange method for the preparation of a second or less up to load the noble metal catalyst into the base material including the heart was evenly distributed monofunctional, non-sex reforming catalyst. Catalytic substrate is contacted with an aqueous loading solution containing a precious metal cation and a non-noble metal cation. Load the solution, when the load is complete, the equivalent weight of without being ion bonded to the zeolite non-noble metal cations left in the catalyst, the noble metal cations are 1.2 equivalents of the non-noble metal cations replace from the zeolite when the ion exchange into the zeolite to 6.0 times , at the same time the end point pH of the loading solution is formulated to be between 10.0 to 11.5. 1.2 to a ratio of 6.0 is required is achieved when the molar ratio of the noble metal is added to the non-noble metal cations added to the loading solution for loading a solution of from 1 to 10. The amount of the debris material reduction in the fine pores of the zeolite, the zeolite catalyst is produced in accordance with the use of the ion exchange method.
机译:本发明提供了一种离子交换方法,用于制备第二次或更少以将贵金属催化剂负载到包括心脏在内的基础材料中的均匀分布的单官能,非性别重整催化剂。催化底物与包含贵金属阳离子和非贵金属阳离子的负载水溶液接触。加载溶液后,加载完成后,当量重量为不与催化剂中残留的沸石非贵金属阳离子发生离子键合时,贵金属阳离子为当量非贵金属阳离子从沸石中替代时的1.2当量离子交换到沸石中达到6.0倍,同时上样溶液的终点pH设定为10.0至11.5。当将贵金属与非贵金属阳离子的摩尔比加至加料溶液中以负载1至10的溶液时,需要达到1.2至6.0的比率。在沸石的细孔中,根据离子交换方法的使用来生产沸石催化剂。

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