Novel CHA molecular sieve synthesis method and preparation of SCR catalyst thereof
A synthesis method and molecular sieve technology, applied in molecular sieve catalysts, separation methods, physical/chemical process catalysts, etc., can solve the problems of low activity and achieve the effects of overcoming limitations, good hydrothermal stability, and broad application prospects
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Embodiment 1
[0068] A kind of CHA type SSZ-13 molecular sieve and catalyst preparation method:
[0069]1) 45.59g HY molecular sieve (silicon aluminum ratio nSiO 2 / nAl 2 o 3 =5.20, dry basis 78.1%), 26.68g NaOH sheet alkali, 69.98g deionized water after fully dissolving and dispersing, obtain the slurry component molar ratio to be nNa 2 O:nSiO 2 :nAl 2 o 3 :nOH - :nH 2 O=0.75:1.0:0.192:1.5:10, aged at 85°C for 36 hours to obtain a silica-alumina gel;
[0070] 2) Add 507.51g of silica gel solution (Na 2 O: 0.24wt%, SiO 2 : 30.36wt%), 173.23g N,N,N-dimethylethylcyclohexyl ammonium hydroxide (concentration 20wt%, represented by OSDA1, CAS: 105197-93-1), 25.21gN-methyl-N' -Ethyl-2-azabicyclo[2,2,1]heptane ammonium hydroxide (concentration 25wt%, represented by OSDA2, CAS: 801148-51-6), 56.31g NaOH caustic soda and 218.84g deionized water Thoroughly and ultrasonically stir to mix evenly, add 5% HCl solution to adjust the nOH in the system - / nSiO 2 Ratio, making the mixed slurry co...
Embodiment 2
[0075] The process method of synthesizing CHA type SSZ-13 molecular sieve is similar to embodiment 1, difference is step 1) and step 2) in the mol ratio of mixed sol, the kind of organic template agent, the kind of silicon source, the kind of transcrystalline zeolite and Silicon-aluminum ratio, crystallization temperature and crystallization time, etc., step 3) take 50.0g of H-type SSZ-13 molecular sieve, adopt different soluble metal salt types, concentrations, solution volumes and metal loadings, and take 40.0g in step 4) g copper modified CHA type SSZ-13 molecular sieve, and 20.0g silica sol (SiO 2 content: 30.0wt%) and 66.72g deionized water were evenly mixed to make a catalyst slurry with a solid content of 36.3wt%, which was coated on the cordierite structured material by dipping method. Specific parameters in this embodiment are shown in Table 1, Table 2, Table 3 and Table 4.
Embodiment 3
[0077] The process method of synthesizing CHA type SSZ-13 molecular sieve is similar to embodiment 1, difference is step 1) and step 2) in the mol ratio of mixed sol, the kind of organic template agent, the kind of silicon source, the kind of transcrystalline zeolite and Silicon-aluminum ratio, crystallization temperature and crystallization time, etc., step 3) take 50.0g of H-type SSZ-13 molecular sieve, adopt different soluble metal salt types, concentrations, solution volumes and metal loadings, and take 40g in step 4) Copper modified CHA type SSZ-13 molecular sieve, with 20.0g silica sol (SiO 2 content: 30.0wt%) and 74.90g of deionized water were evenly mixed to make a catalyst slurry with a solid content of 34.1wt%, which was coated on the cordierite structured material by dipping method. Specific parameters in this embodiment are shown in Table 1, Table 2, Table 3 and Table 4.
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