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SCR (Selective Catalytic Reduction) denitration catalyst and preparation method thereof

A denitration catalyst and catalyst technology, which are applied in chemical instruments and methods, separation methods, dispersed particle separation, etc., can solve the problem that the control of active component loading is prone to deviation accumulation, large deviation between content and design value, and long preparation process. and other problems, to achieve the effect of shortening the preparation time, stable slurry properties, and large coating load

Inactive Publication Date: 2013-04-03
CHENGDU DONGFANG KWH ENVIRONMENTAL PROTECTION CATALYSTS
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

No matter whether the coating is prepared first and then the active component is loaded, or the active component is loaded first to make a catalyst powder and then the feed solution is prepared for coating, it is necessary to carry out two roasting treatments, which not only causes energy consumption waste, and the preparation process is long. In the preparation process, the control of the coating amount and the control of the loading amount of active components are prone to deviation accumulation, which leads to a large deviation between the content of each component of the final product and the design value.

Method used

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  • SCR (Selective Catalytic Reduction) denitration catalyst and preparation method thereof
  • SCR (Selective Catalytic Reduction) denitration catalyst and preparation method thereof
  • SCR (Selective Catalytic Reduction) denitration catalyst and preparation method thereof

Examples

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Embodiment 1

[0029] Rinse two cordierite carriers of 200 mesh and 400 mesh 150mm*150mm*100mm with deionized water, and then dry them at 120°C for 5 hours for later use. Mix 2000g of anatase titanium dioxide, 200g of pseudoboehmite, and 200g of cerium-zirconium solid solution powder, and then control the average particle size at 5.6um after gas crushing; add 120g of ammonium tungstate (calculated as tungsten trioxide ), 7.2g of vanadium oxalate (calculated as vanadium pentoxide) and 9600g of deionized water, aged for 3h and then emulsified for 30min; the solid content of the prepared liquid was 20%, the viscosity was 235mPa·S, and the pH value was 2.3. The prepared slurry was coated on the surface of the carrier by negative pressure coating and positive pressure extraction, dried at 120°C for 4 hours, and then placed in a muffle furnace to raise the temperature to 550°C at a rate of 2°C / min Calcined for 5 hours to obtain the finished coated SCR denitration catalyst. Its product data is as ...

Embodiment 2

[0032] Rinse two cordierite carriers of 200 mesh and 400 mesh 150mm*150mm*100mm with deionized water, and then dry them at 120°C for 5 hours for later use. Mix 2000g of anatase titanium dioxide, 600g of pseudoboehmite, and 200g of cerium-zirconium solid solution powder, and then control the average particle size at 10.2um after gas crushing; add 120g of ammonium tungstate (calculated as tungsten trioxide ), 7.2g of vanadium oxalate (calculated as vanadium pentoxide) and 9600g of deionized water, aged for 3h and then emulsified for 30min; the solid content of the prepared liquid was 22.6%, the viscosity was 3548mPa·S, and the pH value was 3.5. The prepared slurry was coated on the surface of the carrier by negative pressure coating and positive pressure extraction, dried at 120°C for 4 hours, and then placed in a muffle furnace to raise the temperature to 550°C at a rate of 2°C / min Calcined for 5 hours to obtain the finished coated SCR denitration catalyst. Its product data is...

Embodiment 3

[0036]Rinse two cordierite carriers of 200 mesh and 400 mesh 150mm*150mm*100mm with deionized water, and then dry them at 120°C for 5 hours for later use. Mix 2000g of anatase titanium dioxide, 200g of pseudoboehmite, and 400g of cerium-zirconium solid solution powder, and control the average particle size at 9.7um after gas crushing; add 120g of ammonium tungstate (calculated as tungsten trioxide) to the mixed powder ), 7.2g of vanadium oxalate (calculated as vanadium pentoxide) and 9600g of deionized water, aged for 3h and then emulsified for 30min; the solid content of the prepared liquid was 21.3%, the viscosity was 1125mPa·S, and the pH value was 3.5. The prepared slurry was coated on the surface of the carrier by negative pressure coating and positive pressure extraction, dried at 120°C for 4 hours, and then placed in a muffle furnace to raise the temperature to 550°C at a rate of 2°C / min Calcined for 5 hours to obtain the finished coated SCR denitration catalyst. Its p...

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Abstract

The invention discloses an SCR (Selective Catalytic Reduction) denitration catalyst and a preparation method thereof. The catalyst consists of the following components in parts by weight: 100 parts of titanium dioxide, 10-30 parts of pseudo-boehmite, 10-20 parts of rare-earth oxides, 1-15 parts of ammonium tungstate and 0.1-5 parts of vanadium oxalate. The preparation method comprises the following steps: directly adding catalysis active components in slurry of a coating material, so as to form the composite slurry containing the catalysis active components; coating the composite slurry on the surface of an integrated type honeycomb carrier; and finally, drying and roasting to obtain the SCR denitration honeycomb catalyst. According to the invention, coating preparation and active component loading can be completed by one step; through detection, the catalyst has the characteristics of high activity and wide active temperature window; the active components are sufficiently adhered to the surface of powder of the coating after being aged, so that the purpose of accurately controlling the catalysis active components can be realized; and a method for controlling the grain size of the powder and emulsifying the slurry at a high speed is adopted, so that the properties of the slurry are more stable, the load amount of the coating is larger, and the combination is firmer.

Description

technical field [0001] The invention belongs to the technical field of catalyst preparation, in particular to the technical field of SCR (Selective Catalytic Reduction, SCR) denitrification catalyst preparation, and in particular to a coated integral SCR denitration honeycomb catalyst and a preparation method thereof. Background technique [0002] Nitrogen oxides are one of the main pollutants in the atmosphere. When the conditions are suitable, photochemical reactions occur under sunlight, which can suffocate people in a wide range and cause potential harm to the ecological environment. my country has clearly listed NOx emissions as one of the key pollutants to be controlled during the period, and accordingly promulgated corresponding nitrogen oxide control policies for large emitters such as thermal power industry and motor vehicle industry. [0003] There are two main sources of NOx emissions, namely stationary sources such as coal-fired power plants, cement plants, glass...

Claims

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Application Information

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IPC IPC(8): B01J23/30B01D53/90B01D53/56
Inventor 廖新崔文伟艾生炳梁材代华均王尚琛陈凯熊丽仙
Owner CHENGDU DONGFANG KWH ENVIRONMENTAL PROTECTION CATALYSTS