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Manganese-zirconium dual metal modified selective catalytic reduction catalyst for molecular sieve type diesel engine

A molecular sieve, bimetallic technology, applied in molecular sieve catalysts, physical/chemical process catalysts, mechanical equipment, etc., can solve the problems of vanadium-based catalysts that are more harmful to human health, small effective temperature window, catalyst loss, etc., to achieve flexible composition ratios Adjustable, increase metal loading, and improve the effect of low temperature activity

Inactive Publication Date: 2013-05-08
TIANJIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The current commercialized SCR catalysts are mainly based on V 2 o 5 The supported catalyst as the main catalyst has a small effective temperature window, especially the minimum effective temperature is around 300°C, which is difficult to meet the actual requirements for low-temperature activity of SCR catalysts for diesel vehicles operating on Chinese urban roads
At the same time V 2 o 5 It is a highly toxic substance. Because the catalyst will inevitably be lost during use, the vanadium-based catalyst is harmful to human health.

Method used

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  • Manganese-zirconium dual metal modified selective catalytic reduction catalyst for molecular sieve type diesel engine
  • Manganese-zirconium dual metal modified selective catalytic reduction catalyst for molecular sieve type diesel engine
  • Manganese-zirconium dual metal modified selective catalytic reduction catalyst for molecular sieve type diesel engine

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Experimental program
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Effect test

preparation example Construction

[0020] The preparation method of this catalyst modification comprises the following steps:

[0021] (1) 4~7g manganese nitrate (molecular formula: Mn(NO 3 ) 2 4H 2 O; molecular weight: 251.01) and 4-15g zirconium nitrate (molecular formula: Zr(NO 3 ) 4 ·5H 2 (2; Molecular weight: 429.32) is dissolved in 200ml deionized water, then weighing 15~18.5g model is H / ZSM-5, the molecular sieve powder that silicon aluminum ratio is 16: 1 joins in the mixed solution of manganese nitrate and zirconium nitrate, Reflux and stir in a water bath at 70-80°C for 4-6 hours for ion exchange;

[0022] (2) Remove the reflux condensing device in the ion exchange step and continue to heat, stir and impregnate at 70-80°C until the liquid components are evaporated to dryness;

[0023] (3) Dry the ion-exchanged-impregnated solid powder at 90-110° C. for 12-24 hours, and then calcinate at 550-650° C. for 2-3 hours.

[0024] The NOx catalytic activity evaluation test of embodiment 1~4 modified mol...

Embodiment 1

[0030] (1) Modification

[0031] Dissolve 5.8g of manganese nitrate and 4.3g of zirconium nitrate in 200ml of deionized water, then weigh 17.9g of molecular sieve powder with the type H / ZSM-5 and a silicon-aluminum ratio of 16:1 and add it to the mixed solution of manganese nitrate and zirconium nitrate , and reflux and stir in a water bath at 70°C for 6h for ion exchange. Then remove the reflux condensing device, and continue to heat and stir at 70°C for impregnation until the liquid component evaporates to dryness. The ion-exchanged-impregnated solid powder was dried at 100°C for 16h, and then calcined at 550°C for 3h.

[0032] (2) load

[0033] It is determined to coat 5-6% of the coating on 1 kg of cordierite honeycomb ceramic carrier.

[0034] 20g γ-Al is required for every 100g modified molecular sieve powder 2 o 3 , 5g pseudo-boehmite, 10g cerium-zirconium, 5g polyethylene glycol (average molecular weight 4000) and 50g nitric acid ratio, weigh modified molecular siev...

Embodiment 2

[0040] (1) Modification

[0041] 5.5 g of manganese nitrate and 8 g of zirconium nitrate were dissolved in 200 ml of deionized water. Then weigh 17.2g of molecular sieve powder of type H / ZSM-5, with a silicon-aluminum ratio of 16:1, add it to the mixed solution of manganese nitrate and zirconium nitrate, and reflux and stir in a water bath at 80°C for 4 hours to carry out ion exchange. Then remove the reflux condensing device, and continue heating and stirring at 80°C for impregnation until the liquid component evaporates to dryness. The ion-exchanged-impregnated solid powder was dried at 90°C for 24h, and then calcined at 600°C for 3h.

[0042] (2) load

[0043] It is determined to coat 10-11% of the coating on 1 kg of cordierite honeycomb ceramic carrier.

[0044] 20g γ-Al is required for every 100g modified molecular sieve powder 2 o 3 , 5g pseudo-boehmite, 10g cerium-zirconium, 5g polyethylene glycol (average molecular weight 4000) and 50g nitric acid ratio, weigh mod...

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Abstract

The invention discloses a manganese-zirconium dual metal modified selective catalytic reduction catalyst for a molecular sieve type diesel engine. In the catalyst, manganese and zirconium elements enter a molecular sieve by a liquid ion exchange-immersion method; by taking the total weight of the modified powdered catalyst as reference, the manganese element accounts for 4.5 to 7.5 percent, and the zirconium element accounts for 4.5 to 15 percent; by taking the total weight of a supported catalyst as reference, a coating accounts for 5 to 15 percent; urea or ammonia is adopted as a reducing agent to remove NOx in exhaust gas of the diesel engine by virtue of selective catalytic reduction reaction; the novel SCR (selective catalytic reduction) catalyst for the diesel vehicle is prepared from non-toxic molecular sieve and low-toxic manganese and zirconium elements, so that the toxicity of the catalyst to a human body is reduced; and simultaneously a high-activity temperature window of the catalyst in the SCR reaction of the diesel vehicle is enlarged. According to the modification method, the supporting capacity is improved, the supporting proportion is more flexible and adjustable,and further optimization of the catalyst performance is facilitated.

Description

technical field [0001] The invention belongs to a purification catalyst for diesel engines, in particular to a molecular sieve type catalyst for diesel engines modified by manganese and zirconium bimetals. Background technique [0002] At present, the exhaust emission of vehicle diesel engine is one of the important pollution sources, and the nitrogen oxide (NOx) and particulate matter (PM) emitted by it seriously endanger human health. Since it is difficult to reduce NOx and PM emissions at the same time by improving the combustion in the cylinder, the exhaust after-treatment technology has become an inevitable choice for diesel engine emission control. The Selective Catalytic Reduction (SCR) technology using urea or ammonia as the reducing agent has extremely high NOx purification efficiency, and through matching and optimizing combustion improvement measures, it can also reduce PM emissions and engine fuel consumption at the same time. One of the promising efficient post...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/48B01D53/56B01D53/94F01N3/24
CPCY02A50/20Y02C20/10
Inventor 宋崇林吕刚宾峰张清茂
Owner TIANJIN UNIV
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