Selective catalytic reduction catalyst based on copper-vanadium bimetallic modified molecular sieve and preparation method thereof

A molecular sieve and bimetallic technology, applied in the field of selective catalytic reduction catalyst and preparation based on copper-vanadium bimetallic modified molecular sieve, can solve the problem that the catalytic activity of copper or iron modified molecular sieve type catalyst is not improved at high temperature and low temperature activity It can improve the catalytic activity of low-temperature SCR reaction, reduce the harm to the environment and human health, and enhance the oxygen storage performance.

Inactive Publication Date: 2018-04-20
HEFEI SHENZHOU CATALSIS PURIFIER CO LTD
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  • Summary
  • Abstract
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  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This type of catalyst has better catalytic performance for SCR reaction at a reaction temperature of 300-450 °C, and the above-mentioned catalytic activity temperature window is more suitable for national IV and national V diesel engines that mainly operate at high speeds and are not highly strengthened. High-temperature activity is poor, vanadium-based catalysts are not suitable for diesel vehicles running on urban roads (crowded roads, slow motor vehicles, relatively low exhaust temperature) and highly enhanced diesel engines (exhaust temperature > 450 ℃, relatively high); at the same time, V as the main active component in vanadium-based catalysts 2 o 5 It is a highly toxic substance, and it is loaded with a large dose of V in the SCR catalyst 2 o 5 It will inevitably endanger the environment and safety; in addition, WO must be added to the vanadium-based catalyst 3 or MoO 3 As a phase transition stabilizer, slowing down the TiO 2 The transition from anatase crystal phase to rutile crystal phase leads to complex catalyst preparation process and increased production cost
On the other hand, the United States, Japan and other developed countries have begun to use copper or iron element modified molecular sieve SCR catalysts on vehicle diesel engines. This type of catalyst has achieved certain improvements in the catalytic activity of low-temperature SCR reactions. (T50) drops to about 250°C, but it is still difficult to meet the demand for diesel vehicles running on urban roads in my country (T50 should be lower than 230°C), and the high-temperature SCR reaction catalytic activity of copper or iron-modified molecular sieve catalysts has not improved. , and cannot meet the needs of domestic high-strength diesel engines

Method used

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  • Selective catalytic reduction catalyst based on copper-vanadium bimetallic modified molecular sieve and preparation method thereof
  • Selective catalytic reduction catalyst based on copper-vanadium bimetallic modified molecular sieve and preparation method thereof
  • Selective catalytic reduction catalyst based on copper-vanadium bimetallic modified molecular sieve and preparation method thereof

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Embodiment 1

[0043] A method for preparing a selective catalytic reduction catalyst based on copper-vanadium bimetallic modified molecular sieves, prepared through the following steps:

[0044] (1) Determination of the amount of raw materials

[0045] The mass percentages of main active ingredients, auxiliary active ingredients and coating auxiliary materials are: 20%: 15%: 65%;

[0046] Among them, CuO, V 2 o 5 And the mass percent of ZSM-5 type molecular sieve is 5%: 5%: 90%;

[0047] Co-active ingredient CeO 2 and ZrO 2 The mass percentage is 90%:10%;

[0048] Among coating auxiliary materials, γ-Al 2 o 3 with SiO 2 The mass percentage is 60%: 40%;

[0049] Pure γ-Al in Coating Auxiliary Materials 2 o 3 Convert with aluminum sol to generate γ-Al 2 o 3 The mass percentage is 75%: 25%;

[0050] Every mole of ammonium metavanadate needs 2 moles of oxalic acid; every 100g of catalytic coating needs 10g of polyethylene glycol with an average molecular weight of 20000 and 50g of...

Embodiment 2

[0065] (1) Determination of the amount of raw materials

[0066] The mass percentages of main active ingredients, auxiliary active ingredients and coating auxiliary materials are: 25%: 15%: 60%;

[0067] Among them, CuO, V 2 o 5 And the mass percent of ZSM-5 type molecular sieve is 16%: 4%: 80%;

[0068] Co-active ingredient CeO 2 and ZrO 2 The mass percentage is 60%: 40%;

[0069] Among coating auxiliary materials, γ-Al 2 o 3 with SiO 2 The mass percentage is 80%:20%;

[0070] Pure γ-Al in Coating Auxiliary Materials 2 o 3 Convert with aluminum sol to generate γ-Al 2 o 3 The mass percentage is 60%: 40%;

[0071] Every mole of ammonium metavanadate needs 3 moles of oxalic acid; every 100g of catalytic coating needs 5g of polyethylene glycol with an average molecular weight of 20000 and 25g of nitric acid; every 100g of copper-vanadium bimetallic modified molecular sieve needs 200ml of n-hexane; 2000g The amount of raw materials required for catalytic coating is: ...

Embodiment 3

[0086] (1) Determination of the amount of raw materials

[0087] The mass percentages of main active ingredients, auxiliary active ingredients and coating auxiliary materials are: 10%:10%:80%;

[0088] Among them, CuO, V 2 o 5 And the mass percent of ZSM-5 type molecular sieve is 10%: 10%: 80%;

[0089] Co-active ingredient CeO 2 and ZrO 2 The mass percentage is 80%:20%;

[0090] Among coating auxiliary materials, γ-Al 2 o 3 with SiO 2 The mass percentage is 75%: 25%;

[0091] Pure γ-Al in Coating Auxiliary Materials 2 o 3 Convert with aluminum sol to generate γ-Al 2 o 3 The mass percentage is 60%: 40%;

[0092] Every mole of ammonium metavanadate needs 2 moles of oxalic acid; every 100g of catalytic coating needs 8g of polyethylene glycol with an average molecular weight of 20,000 and 40g of nitric acid; every 100g of copper-vanadium bimetallic modified molecular sieve needs 300ml of n-hexane; 2000g The amount of raw materials required for catalytic coating is: ...

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Abstract

The invention discloses a selective catalytic reduction catalyst based on a copper-vanadium bimetallic modified molecular sieve and a preparation method thereof. In the catalyst, a copper-vanadium bimetallic modified molecular sieve is taken as a main active component, CeO2 and ZrO2 are taken as auxiliary active ingredients, gamma-Al2O3 and SiO2 construct a coating auxiliary material, and 400-meshcordierite honeycomb ceramics is taken as a catalyst carrier. A preparation process comprises: determination of the using amounts of raw materials, preparation of the copper-vanadium bimetallic modified molecular sieve and preparation and coating of coating slurry. The advantages of high catalysis activity and high dispersity of a copper modified molecular sieve catalyst in a low-temperature SCR(Selective Catalytic Reduction) reaction and the advantage of high catalysis activity of V2O5 in a high-temperature SCR reaction can be brought into play at the same time; meanwhile, the using amountof the V2O5 is reduced, and the toxicity of the catalyst is lowered; the coating auxiliary material consisting of the gamma-Al2O3 and the SiO2 can improve the thermal stability and mechanical strengthof a catalytic coating, and the dispersion uniformity of the active components; through addition of the CeO2 serving as the auxiliary active component, the catalysis activity of the catalyst in the low-temperature SCR reaction is enhanced.

Description

technical field [0001] The invention belongs to the technical field of diesel engine tail gas purification, and in particular relates to a selective catalytic reduction catalyst based on copper-vanadium bimetallic modified molecular sieves and a preparation method thereof. Background technique [0002] Diesel engines for vehicles are widely used in the field of heavy-duty passengers and trucks due to their advantages such as high output power, high thermal efficiency, and durability, bringing great convenience to industrial and agricultural production and people's lives. However, due to the limitation of the combustion method, the NOx emission of the diesel engine is relatively large, which has caused serious harm to the atmospheric environment and human health. Especially with the rapid growth of the number of diesel vehicles in my country in recent years, the total NOx emissions of diesel vehicles and their contribution to the total atmospheric NOx emissions have also incr...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/48B01D53/94B01D53/56
CPCB01D53/9413B01D2255/2065B01D2255/20715B01D2255/20723B01D2255/20761B01D2255/2092B01D2255/30B01D2255/504B01J29/48
Inventor 胡朝稳吕颂
Owner HEFEI SHENZHOU CATALSIS PURIFIER CO LTD
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