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Modified CHA molecular sieve and preparation method and application thereof

A molecular sieve and modification technology, which is applied in the direction of separation methods, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of reducing pore volume, catalyst deactivation, hindering the contact between reactants and active centers, etc., and achieve high pore volume, increase Effect of large pore volume and specific surface area, high crystallinity

Active Publication Date: 2020-01-10
SHANDONG SINOCERA FUNCTIONAL MATERIAL CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The above various such as (NH 4 ) 2 SO 4 or NH 4 HSO 4 and CuSO 4 and other sulfur-containing compounds, along with NH 3 - The use of SCR catalyst gradually accumulates in the pores of Cu-CHA molecular sieve, reducing its pore volume, covering its acid sites, hindering the contact of reactants with active centers, and finally leading to catalyst deactivation

Method used

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  • Modified CHA molecular sieve and preparation method and application thereof
  • Modified CHA molecular sieve and preparation method and application thereof
  • Modified CHA molecular sieve and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0077] Example 1 H-SSZ-13 molecular sieves A1, A2, A3, A4, A5, A6 and A7 (H-CHA molecular sieves before modification)

[0078] Add 126.0g of 25% N,N,N-trimethylamantadine hydroxide to 23.5g of deionized water, mix well, then add 3.1g of sodium hydroxide to it, stir until fully dissolved, then 5.3g of hydroxide Aluminum (Al 2 o 3 The content is 65%), mix well, and finally add 150.0g of silica sol (SiO 2 content of 30%), fully stirred for 2h to obtain the primary mixture. Wherein, the Al in the primary mixture 2 o 3 , SiO 2 , N,N,N-Trimethylamantadine Hydroxide, OH - and H 2 The molar ratio of O is 1:22.21:4.45:6.70:366.42. The above mixture was transferred to a stainless steel reaction kettle lined with polytetrafluoroethylene, placed in a 170 °C oven for crystallization for 48 hours, taken out, quenched, and the crystallized product was subjected to solid-liquid separation, washing and drying to obtain Na- SSZ-13 molecular sieve (initial molecular sieve).

[0079] Am...

Embodiment 2

[0081]Example 2 H-SSZ-13 molecular sieves CA1, CA2, CA3, CA4, CA5, CA6 and CA7

[0082] The H-SSZ-13 molecular sieves A1, A2, A3, A4, A5, A6 and A7 prepared in Example 1 were subjected to acid treatment. where SiO 2 / Al 2 o 3 H-SSZ-13 molecular sieves A1-A4 less than 30 are divided into the first group, SiO 2 / Al 2 o 3 H-SSZ-13 molecular sieves A5-A7 larger than 30 belong to the second group.

[0083] The acid treatment conditions were the same for the first set of samples. Taking H-SSZ-13 molecular sieve A1 as an example to illustrate the acid treatment conditions of the first group of samples, add 100g of H-SSZ-13 molecular sieve A1 into 1000mL of 0.3mol / L hydrochloric acid solution and stir at 65°C for 30min, then perform solid-liquid separation , washed and dried to obtain H-SSZ-13 molecular sieve CA1, whose SiO 2 / Al 2 o 3 =20.39. The acid treatment conditions of H-SSZ-13 molecular sieves A2-A4 are the same as those of H-SSZ-13 molecular sieves A1, H-SSZ-13 mol...

Embodiment 3

[0085] Example 3 H-SSZ-13 molecular sieves DA1, DA2, DA3, DA4, DA5, DA6 and DA7 (modified CHA molecular sieves)

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PUM

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Abstract

The invention relates to a modified CHA molecular sieve, and a preparation method and application thereof, in particular to the application to the exhaust gas treatment of diesel vehicles, and belongsto the field of catalytic materials. The molar ratio of silica to alumina in the modified CHA molecular sieve is 24.5 to 36; the pore volume of the modified CHA molecular sieve is not less than 0.32cm<3> / g; the crystallinity of the modified CHA molecular sieve is not more than 5% lower than that of a pre-modified H-CHA molecular sieve, the initial CHA molecular sieve is subjected to ammonium ionexchange and first calcinations to prepare the pre-modified H-CHA molecular sieve, and then is subjected to acid treatment and alkali treatment to prepare the modified CHA molecular sieve. The crystallinity of the modified Cu containing CHA molecular sieve prepared by copper exchange of the modified CHA molecular sieve is high, thus the service life of the modified Cu containing CHA molecular sieve as a catalyst in the selective reduction of ammonia is prolonged; and the pore volume of the modified Cu containing CHA molecular sieve is large, more materials which can cause the blockage of catalyst pore channel and reduction of pore volume can be accommodated, and thus the service life of the catalyst is prolonged.

Description

technical field [0001] The application relates to a modified CHA molecular sieve and its preparation method and application, especially the application in the treatment of diesel vehicle tail gas, which belongs to the field of catalytic materials. Background technique [0002] Nitrogen oxides (NOx) are serious air pollutants, and diesel vehicle exhaust emissions are one of the main sources of NOx. In order to meet the escalating emission standards, the treatment of diesel vehicle exhaust has become increasingly important and urgent. Selective catalytic reduction of ammonia (NH 3 -SCR) is currently a widely used after-treatment strategy for diesel vehicle exhaust NOx. [0003] Copper-exchanged Cu-CHA molecular sieve is currently recognized as the most effective ammonia selective catalytic reduction (NH for short) for diesel vehicle exhaust treatment. 3 -SCR) catalyst. From the perspective of economy and convenience, diesel vehicle exhaust treatment NH 3 -The SCR process ...

Claims

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Application Information

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IPC IPC(8): B01J29/72B01J35/10B01D53/94B01D53/56
CPCB01J29/723B01D53/9418B01J2229/18B01J2229/37B01J2229/38B01J35/617B01J35/633
Inventor 宋锡滨张军亮潘光军焦英训
Owner SHANDONG SINOCERA FUNCTIONAL MATERIAL CO LTD
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