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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

Inactive Publication Date: 2020-11-03
CHINA CATALYST HLDG CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The technical problem to be solved by the present invention is to overcome the SCR catalyst using synthetic molecular sieves loaded with iron and copper in the prior art to be active at low temperatures through the hydrothermal durability test. Lower defects, providing a copper-based SCR catalyst with high activity at low temperature after hydrothermal durability test and its preparation method

Method used

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  • CHA type molecular sieve for purifying diesel vehicle tail gas, catalyst, preparation method and application
  • CHA type molecular sieve for purifying diesel vehicle tail gas, catalyst, preparation method and application
  • CHA type molecular sieve for purifying diesel vehicle tail gas, catalyst, preparation method and application

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Experimental program
Comparison scheme
Effect test

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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Abstract

The invention discloses a CHA type molecular sieve for purifying diesel vehicle tail gas, a catalyst, a preparation method and application, and belongs to the field of chemical synthesis technology and application thereof. The CHA-type aluminosilicate zeolite molecular sieve is synthesized by adopting an N,N,N-trimethyl-3,3,5-trimethylcyclohexyl quaternary ammonium onium compound as an organic template agent, wherein the molar ratio of silicon dioxide to aluminum oxide is 6-80, the average grain diameter is less than or equal to 500nm, the total specific surface area is more than or equal to 400m2 / g, the total pore volume is more than or equal to 0.20 ml / g, the micropore volume is more than 0.10 ml / g, and thecrystal grain diameter in the crystal face (-210) direction is 50-160 nm. After the molecular sieve is subjected to hydro-thermal treatment at 600-850 DEG C, the tetra-coordinated aluminum accounts for more than or equal to 90% of the total aluminum amount, and the hexa-coordinatedaluminum accounts for less than or equal to 10% of the total aluminum amount. The molecular sieve provided by the invention has high hydrothermal stability under the condition of no large crystal grains, and shows high nitrogen oxide reduction characteristics after being exposed at high temperature and high humidity, especially shows high nitrogen oxide reduction characteristics in a temperaturerange of 200-550 DEG C.

Description

technical field [0001] The invention relates to a CHA-type molecular sieve used for purifying diesel vehicle tail gas, a catalyst, a preparation method and application, and belongs to the field of chemical synthesis technology and its application. Background technique [0002] The silica-alumina zeolite molecular sieve is a CHA-type topological structure with a three-dimensional pore structure and orthogonal symmetry. The one-dimensional main channel is composed of double eight-membered rings, the pore size is 0.38nm×0.38nm, and the skeleton density is 14.5. The topological structure of CHA molecular sieve is composed of double 6 rings (d6r) connected by 4-membered rings to form a large cha cage. The d6r crystal plane faces the cha large cage. Cu ions can be stabilized in d6r at high temperature, allowing Cu ions to migrate. It is also the unique physical and chemical characteristics of small-pore molecular sieves with SCR reaction potential. In the literature (J.Phys.Chem....

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/76C01B39/02C01B39/48B01D53/86B01D53/56B01D53/94
CPCB01J29/763C01B39/48C01B39/026B01D53/8628B01D53/9413C01P2002/72C01P2004/03C01P2006/12C01P2006/14C01P2004/62B01D2251/2062B01D2251/2067B01J2229/186
Inventor 王志光王炳春史振宇李进柳海涛
Owner CHINA CATALYST HLDG CO LTD
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