CHA type molecular sieve for purifying diesel vehicle tail gas, catalyst, preparation method and application
A technology for exhaust gas purification and molecular sieve, which can be used in molecular sieve catalysts, molecular sieves and alkali exchange compounds, physical/chemical process catalysts, etc., and can solve problems such as low activity
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Embodiment 1
[0065] A kind of preparation method of CHA type SSZ-13 molecular sieve and SCR catalyst:
[0066] 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 :nH 2 O=0.75:1.0:0.192:10, aged in a crystallization kettle at 85°C for 36 hours to obtain a silica-alumina gel;
[0067] 2) Add 507.51g of silica gel solution (Na 2 O: 0.24wt%, SiO 2 : 30.36wt%), 275.29g N,N-diethyl-N'-methyl-3,3,5-trimethylcyclohexyl ammonium hydroxide (concentration 20wt%, represented by OSDA), 56.31g NaOH sheet Alkali, 21.25g NaCl and 156.10g deionized water are fully mixed with ultrasonic stirring, so that the molar ratio of the mixed slurry components is nNa 2 O:nSiO 2 :nA1 2 o 3 :nOSDA:nNaCl:nH 2 O=0.35:1.0:0.0286:0.08:0.12:15; add 5% HCl solution to adjust nOH in the system - / nSiO 2 Ratio...
Embodiment 2
[0072] The process method of synthesizing CHA type SSZ-13 molecular sieve is similar to embodiment 1, and difference is the slurry component molar ratio (nNa 2 O:nSiO 2 :nAl 2 o 3 :nH 2 (0), zeolite molecular sieve type, zeolite molecular sieve silicon-alumina ratio, aging temperature and aging time, step 2) in the mixed slurry component molar ratio, organic template type, type of silicon source, seed crystal addition amount, acid type added , metal salt M type, crystallization temperature and crystallization time, step 4) get H-type SSZ-13 molecular sieve 50.0g, adopt different soluble metal salt types, concentrations, solution volumes and metal loads, and step 5) take 40.0g copper modified CHA type SSZ-13 molecular sieve, and 20.0g silica sol (SiO 2 content: 30.0wt%) and 97.53g deionized water were uniformly mixed to make a catalyst slurry with a solid content of 29.2wt%, which was coated on the cordierite structured material by dipping method. Specific parameters in th...
Embodiment 3
[0074] The process method of synthesizing CHA type SSZ-13 molecular sieve is similar to embodiment 1, and difference is the slurry component molar ratio (nNa 2 O:nSiO 2 :nAl 2 o 3 :nH 2 (0), zeolite molecular sieve type, zeolite molecular sieve silicon-alumina ratio, aging temperature and aging time, step 2) in the mixed slurry component molar ratio, organic template type, type of silicon source, seed crystal addition amount, acid type added , metal salt M type, crystallization temperature and crystallization time, step 4) get H-type SSZ-13 molecular sieve 50.0g, adopt different soluble metal salt types, concentrations, solution volumes and metal loads, and step 5) take 40g copper modified CHA type SSZ-13 molecular sieve, and 20.0g silica sol (SiO 2 content: 30.0wt%) and 88.87g deionized water were evenly mixed to make a catalyst slurry with a solid content of 30.9wt%, which was coated on the cordierite structured material by dipping method. Specific parameters in this embo...
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