Honeycomb catalyst for denitration of glass furnace fume and preparation method thereof

A honeycomb catalyst, glass furnace technology, applied in chemical instruments and methods, physical/chemical process catalysts, separation methods, etc., can solve the problems of short catalyst service life, high catalyst price, high catalyst cost, and achieve water resistance and sulfur resistance. The effect of good performance, excellent denitration activity and strong adsorption capacity

Active Publication Date: 2010-08-04
沈炳龙
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

②In recent years, domestic enterprises have introduced foreign technology, but the scale is small, and the production raw materials still need to be imported
③ The catalyst is expensive, about 50,000 yuan per cubic meter, accounting for about 40% of the entire denitrification project cost
④ The service life of the catalyst is short, and it needs to be replaced in about three years, and the cost of replacing the catalyst every year is also high
⑤ The production capacity of several foreign SCR catalyst production plants is only 100,000 cubic meters per year, which is far from meeting the needs of our country
... In summary, it is not difficult to see that the problems existing in the production and use of catalysts are one of the bottlenecks restricting flue gas denitrification projects
In the previous reducing catalysts, amorphous MnO was also used x , but this amorphous MnO x , it is afraid of water and sulfur, and its activity is poor at low temperature, and these reductive catalysts choose metatitanic acid as raw material, and carry V 2 o 5 After that, it is easy to make the SO in the flue gas 2 converted to SO 3 , which is an undesired result for any catalyst

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0059] Purchase commercially available metatitanic acid as raw material, beat with deionized water, wash and filter to remove unwashed SO 4 root, make SO 4 The root is controlled at 3-4% (with TiO 2 In total), the following percentages are percentages of the total amount of catalyst.

[0060] Get 667g of metatitanic acid after cleaning, wherein TiO The weight ratio is 45%, accounting for 30% of the catalyst weight, adding 2000ml of deionized water for beating, and adding 3% V 2 o 5 Metavanadic acid, this metavanadic acid dissolves metavanadic acid with 5% oxalic acid solution under heating. After the metavanadate oxalic acid solution and metatitanic acid are fully mixed, add 8 mol of ammonia water dropwise to adjust the pH of the solution to 9.0-9.2. Then filter, wash with water, dry, pulverize for later use;

[0061] Get the metatitanic acid mixture 330g of above-mentioned loaded vanadium, account for 33% of catalyst weight, add amorphous MnOx 50g (account for 5...

Embodiment 2

[0066] Get the metatitanic acid after cleaning described in embodiment 1, account for 30% of the total weight of the catalyst, add the amorphous MnO of the total weight of the catalyst 5%. x Fully knead, add 30% TiO by total catalyst weight 2 -SiO 2 Powder, high-viscosity attapulgite with 24% total weight of catalyst and 3% V 2 o 5 Metavanadic acid, and add an appropriate amount of deionized water for kneading. Mix the active ingredients well. Then add hole expansion, lubricant and forming enhancer: 3.5% hydroxypropyl methylcellulose, 3% glass fiber, continue kneading, remove air bubbles in a vacuum mud mixer, and then extrude on the mold to 50× 50×200mm honeycomb carrier, the honeycomb hole is 3×3mm. The carrier was dried and calcined for later use, wherein the drying and calcining were the same as in Example 1.

[0067] Will contain 5% amorphous MnO x , 3% of V 2 o 5 The honeycomb titanium-silicon carrier is immersed in the ammonium metatungstate solution (138.9g / l)...

Embodiment 3

[0071] Take 30% of the washed metatitanic acid, add 2 times the weight of deionized water for beating, and add V 2 o 5 3% metavanadic acid, the metavanadic acid is dissolved with 5% oxalic acid solution under heating. After the metavanadate oxalic acid solution and metatitanic acid are fully mixed, add 8 mol of ammonia water dropwise to adjust the pH of the solution to 9.0-9.2. Then filter, wash with water, dry and pulverize for later use.

[0072] Take 33% metatitanic acid loaded with vanadium, add 5% amorphous MnO x Fully knead, add TiO 2 -SiO 2 20% of powder, 34% of high-viscosity attapulgite, hole expansion, lubricant and forming enhancer: 3% of squid powder, 1.5% of hydroxypropyl methylcellulose, 3.0% of glass fiber, and then kneaded. Air bubbles are removed in a vacuum mud mill, and then extruded on a mold to form a 50×50×200mm honeycomb carrier, the honeycomb pores are 3×3mm, and the carrier is dried and roasted for later use. The drying and roasting are the same a...

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PUM

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Abstract

The invention discloses a honeycomb catalyst for SCR (Selective Catalytic Reduction) denitration of glass furnace fume, which comprises a carrier and active components. The honeycomb catalyst is characterized in that the carrier is a honeycomb titanium-silicon carrier which contains 30-50 wt% of TiO2-SiO2 powder, 10-20 wt% of TiO2 and 20-50 wt% of high-viscosity attapulgite; the active components comprise amorphous MnOx, V2O5 and WO3, wherein the amorphous MnOx accounts for 5-25.0% of the total weight of the catalyst, V2O5 accounts for 0.5-5.0% of the total weight of the catalyst, and WO3 accounts for 0.1-8.0% of the total weight of the catalyst. By adopting the high-viscosity attapulgite, the catalyst has high plasticity, strong binding power and strong water absorption; by selecting the TiO2-SiO2 powder, not only the apparent structures, such as the specific surface, the pore volume and the like, of the carrier can be improved, but also the conversion rate of SO2 to SO3 is inhibited. The selective reducing catalyst can be widely applied to selective reduction of nitrogen oxide in glass furnace fume.

Description

technical field [0001] The invention relates to a catalyst, in particular to a honeycomb catalyst used in selective catalytic reduction (SCR) denitrification of glass kiln flue gas and a preparation method thereof. Background technique [0002] According to statistics: In 2000, the national SO 2 Emissions are about 19.9 million tons, NO x The emission is about 11.7 million tons, and the area of ​​acid rain affects 40% of the country and nearly 4 million square kilometers. This has brought huge economic losses to the national economy, and also severely damaged the environment on which human beings rely for survival [because: ① nitrogen oxides seriously damage the atmospheric ozone layer, ② the affinity between nitrogen nitrides and red blood cells is 1000 times higher than that of carbon monoxide, ③ acid rain directly harms The growth of plants and crops, ④ nitrogen oxides will also affect the quality of groundwater.... With the expansion of comprehensive utilization of so...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/34B01J35/04B01D53/86B01D53/56
Inventor 沈炳龙
Owner 沈炳龙
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