A kind of cu-sapo-34 molecular sieve catalyst, preparation method and application thereof

A technology of cu-sapo-34 and molecular sieve, which is applied in the direction of molecular sieve catalysts, separation methods, chemical instruments and methods, etc., can solve the problems of low crystallinity, small specific surface area and pore volume, and reduced catalytic activity of molecular sieves

Active Publication Date: 2016-08-17
江西中科鸿虔新材料有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, if the copper content is too high, it is easy to form more CuO, and non-selective redox NH 3 , resulting in catalytic activity and N 2 Reduced selectivity
If the calcination temperature is low, the organic amine as the template cannot be completely removed, resulting in low crystallinity of the molecular sieve, small specific surface area and pore volume, and reduced catalytic activity.

Method used

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  • A kind of cu-sapo-34 molecular sieve catalyst, preparation method and application thereof
  • A kind of cu-sapo-34 molecular sieve catalyst, preparation method and application thereof
  • A kind of cu-sapo-34 molecular sieve catalyst, preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0044] Add pseudo-boehmite into deionized water and stir, then add any one of fumed silica or silica sol and orthophosphoric acid, add copper sulfate and tetraethylenepentamine after mixing, add diethylamine after fully stirring , triethylamine or n-propylamine;

[0045] Put the fully stirred gel into a hydrothermal reaction kettle for crystallization at 180°C for 72 hours. After the crystallization reaction is completed, cool at room temperature, separate the solid crystalline product from the mother liquor, wash with deionized water until neutral, and dry at 100°C for 12 hours , and then calcined in air at a calcining temperature of 700°C, a heating rate of 1°C / min during the calcining process, and a calcining time of 5 hours to obtain a Cu-SAPO-34 molecular sieve catalyst.

[0046] Control the consumption of each reactant so that the following mass ratio relationship is possessed in the reaction system:

[0047] al 2 o 3 ,P 2 o 5 , SiO 2 、H 2 O, the molar ratio of co...

Embodiment 2

[0050] Add pseudo-boehmite into deionized water and stir, then add any one of fumed silica or silica sol and orthophosphoric acid, add copper sulfate and tetraethylenepentamine after mixing, add diethylamine after fully stirring , triethylamine or n-propylamine;

[0051] Put the fully stirred gel into a hydrothermal reaction kettle for crystallization at 180°C for 72 hours. After the crystallization reaction is completed, cool at room temperature, separate the solid crystalline product from the mother liquor, wash with deionized water until neutral, and dry at 100°C for 12 hours , and then calcined in air at different temperatures, the heating rate during the calcining process was 1° C. / min, and the calcining time was 5 hours to obtain the Cu-SAPO-34 molecular sieve catalyst.

[0052] In this method, the consumption of each reactant is controlled so that the reaction system has the following mass ratio relationship:

[0053] al 2 o 3 ,P 2 o 5 , SiO 2 、H 2 The mol ratio ...

Embodiment 3

[0056] Add pseudo-boehmite into deionized water and stir, then add any one of fumed silica or silica sol and orthophosphoric acid, add copper sulfate and tetraethylenepentamine after mixing, add diethylamine after fully stirring , triethylamine or n-propylamine;

[0057] Put the fully stirred gel into a hydrothermal reaction kettle for crystallization at 180°C for 72 hours. After the crystallization reaction is completed, cool at room temperature, separate the solid crystalline product from the mother liquor, wash with deionized water until neutral, and dry at 100°C for 12 hours , and then calcined in air at 700° C., the heating rate during the calcining process was 1° C. / min, and the calcining time was 5 hours to obtain the Cu-SAPO-34 molecular sieve catalyst.

[0058] In this method, the consumption of each reactant is controlled so that the following mass ratio relationship is possessed in the reaction system: Al 2 o 3 ,P 2 o 5 , SiO 2 、H 2 O, the molar ratio of coppe...

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Abstract

The invention provides a Cu-SAPO-34 molecular sieve catalyst, a preparation method and an application thereof. The method comprises the following steps: adding pseudo-boehmite into deionized water for stirring, then adding one of fumed silica or silica sol and orthophosphoric acid, adding copper sulfate and tetraethylenepentamine after mixing, fully Add diethylamine, triethylamine or n-propylamine after stirring. Put the fully stirred gel into a hydrothermal reaction kettle for crystallization, then cool at room temperature, separate the solid crystalline product from the mother liquor, wash until neutral, dry, and roast at 600-850°C in air to obtain Cu‑SAPO‑ 34 molecular sieve catalyst. The present invention adopts one-step hydrothermal synthesis method to prepare Cu-SAPO-34 molecular sieve catalyst, and obtains NH 3 ‑SCR molecular sieve catalyst with excellent catalytic activity and hydrothermal stability.

Description

technical field [0001] The invention belongs to the technical field of catalysts, and relates to a Cu-SAPO-34 molecular sieve catalyst, a preparation method and an application thereof. Background technique [0002] Take NH 3 Selective catalytic reduction of NOx or NH as a reducing agent 3 -SCR technology plays an extremely important role in the process of catalytic removal of NOx, and its key core is the development of SCR catalyst system. Due to the characteristics of diesel vehicles with variable operating conditions, large exhaust temperature changes, complex exhaust gas composition, and rapid flow changes, an excellent automotive catalyst must have the following properties: high catalytic activity in a wide temperature window, hydrothermal stability High resistance, high mechanical strength, anti-SO 2 And HC poisoning ability, anti-high airspeed ability and so on. While the current commonly used V 2 o 5 -WO 3 (MoO 3 ) / TiO 2 Although catalysts have been used indu...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/85B01D53/90B01D53/56
Inventor 贺泓牛璨刘福东石晓燕朱龙凤
Owner 江西中科鸿虔新材料有限公司
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