Copper-based SCR catalyst and preparation method thereof
An SCR catalyst, copper-based technology, applied in the field of chemistry, can solve the problems of complicated preparation methods and low catalyst activity, and achieve the effects of low cost and simple preparation process
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[0045]The structurally porous zeolite molecular sieve in the preparation of the SCR catalyst of the present invention, from the single dispersion of copper (II) ions in the framework, the maximum number of oxygen rings is preferably 8 to 12, from the copper (II) ions as The catalyst preferably has a three-dimensional structure in view of retaining a reaction site. In the support of copper (II) ions, hydrogen-type zeolite molecular sieves are usually selected from the viewpoint of durability and heat resistance as a catalyst, and are not particularly limited.
[0046] The zeolite molecular sieves in the preparation of the SCR catalyst of the present invention are exemplified, named according to the structure code of the International Zeolite Association (International Zeolite Association), BEA type structure (such as β as the maximum number of oxygen rings 12), MFI type structure (such as: ZSM-5 with a maximum number of oxygen rings of 10), CHA-type (for example: SSZ-13 with a ...
Embodiment 1
[0088] 1. Synthesis of BEA type zeolite (chemical composition: Na 7 Al 7 Si 57 o 128 ) chemical composition, obtains the BEA type zeolite molecular sieve that ion-exchanges sodium with ammonia. Then calcined at 550°C to obtain the desired BEA-type zeolite molecular sieve.
[0089] 1.1 BEA type synthetic zeolite
[0090] Add aqueous sodium hydroxide solution to colloidal silicon dioxide with a mass fraction of 30%, to obtain a reaction mixture. To this mixture, aluminum nitrate 9 hydrate (Al(NO 3 ) 3 9H 2 O) dissolved in an aqueous solution with a mass fraction of 35% tetraethylammonium hydroxide (TEAOH), obtained after thorough stirring, and the reaction mixture has the following composition.
[0091] 21Na 2 O·10Al 2 o 3 ·300SiO2 2 ·150TEAOH·4000H 2 o
[0092] 1.2 Hydrothermal synthesis
[0093]The above reaction mixture was put into a polytetrafluoroethylene container and heated in an autoclave at a temperature of 155° C. for 3 days. Next, the solid reaction p...
Embodiment 2
[0102] Example 2 is the same as Example 1 except that degassing treatment is not performed, and the Cu-introduced BEA type hydrogenated synthetic zeolite is used as the SCR catalyst.
[0103] The average particle diameter (D50) of the obtained SCR catalyst was 7 μm.
[0104] According to the results of ICP analysis, the copper (II) ion content was 2.3 wt%.
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