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Method and product for increasing SO2 resistance of honeycombed SCR catalyst

A technology of SCR catalyst and honeycomb shape, which is applied in the field of improving the anti-SO2 performance of honeycomb SCR catalyst, which can solve the problems that the SCR reaction cannot continue, cannot be diffused well, and cannot be used in actual industrial applications, so as to promote industrial applications and improve Safety and economy, effect of reducing clogging

Active Publication Date: 2018-08-17
HUAZHONG UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0008] The method of directly applying the patent ZL 2016 1 0225266.5 cannot be used in actual industrial applications
If the idea in patent ZL 2016 1 0225266.5 is used, the molecular sieve is directly coated on the surface of the honeycomb catalyst to prevent SO 2 contact with the SCR catalyst, then due to the N 2 The molecular dynamics diameter is slightly larger than that of SO 2 , so the use of molecular sieve membranes to prevent SO 2 While in contact with the SCR catalyst, the product N of the SCR reaction 2 It also cannot diffuse well, causing the SCR reaction to fail to continue.

Method used

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  • Method and product for increasing SO2 resistance of honeycombed SCR catalyst
  • Method and product for increasing SO2 resistance of honeycombed SCR catalyst
  • Method and product for increasing SO2 resistance of honeycombed SCR catalyst

Examples

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Embodiment 1

[0039] Figure 5 It is a schematic diagram of the structure of Example 1 of the present invention. In this embodiment, the flow layer is coated on the surface of the substrate (cordierite) of the honeycomb SCR catalyst to increase the specific surface area of ​​the substrate and improve the activity of the honeycomb SCR catalyst.

[0040] The honeycomb SCR catalyst described in this embodiment is Mn-Ce-Fe / Al 2 o 3 / cordierite. The purchased cell density is 200-400cell / in 2 cordierite honeycomb ceramics, cut into Size, heat treatment with 10% nitric acid hydrothermal treatment to remove surface impurities, dry and calcined, as the base material of SCR catalyst.

[0041] The circulation layer is formed by coating a porous material, drying and calcining, and the circulation layer in this embodiment is an alumina layer with a thickness of about 10 μm. Mix a certain amount of pseudo-boehmite and urea evenly, add a certain concentration of nitric acid solution, stir at room t...

Embodiment 2

[0047] Example 2 adopts the above-mentioned preferred combination method. In this example, the flow-through layer is coated on the surface of the substrate (cordierite) of the honeycomb SCR catalyst. Cut the purchased cordierite into Size, polished with 2000 mesh sandpaper, washed with deionized water, ethanol, acetone and deionized respectively. Then put it into 20% oxalic acid solution, take it out after a period of water bath treatment, wash and dry it, and use it as the base material of SCR catalyst.

[0048] Prepare an aluminum nitrate solution with a suitable concentration, add an appropriate amount of urea to form an impregnation solution, put the cordierite in the impregnation solution for several hours, take it out, and dry it overnight at 95°C. Continue to keep warm at 110°C for 4h, and then put it into a muffle furnace and bake at 500°C for 8h, with a heating and cooling rate of 2° / min. Repeat the impregnation process until the loading capacity of the alumina flo...

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Abstract

The invention discloses a method and product for increasing the SO2 resistance of a honeycombed SCR catalyst and belongs to the technical field of coal-fired flue gas denitration. The method specifically includes: preparing a micron-thickness circulating layer, used for the flowing of SCR reaction product N2, on the surface of the honeycombed SCR catalyst; coating the outer surface of the circulating layer with a molecular sieve membrane layer for preventing SO2 from contacting with the SCR catalyst; polishing one side, opposite to the inflow direction of flue gas, of a catalyst module to remove the molecular sieve membrane layer on the side so as to allow N2 to be able to flow out from the circulating layer on the side. The method has the advantages that the sieving effect of the molecular sieve membrane layer is utilized to prevent the SO2 from contacting with the honeycombed SCR catalyst, the denitration efficiency of the honeycombed SCR catalyst is unaffected, the SO2 poisoning problem of the honeycombed low-temperature SCR catalyst is solved, and the industrial application of the low-temperature SCR catalyst is promoted.

Description

technical field [0001] The invention belongs to the technical field of coal-fired flue gas denitrification, and more specifically relates to a method for improving the SO2 resistance of a honeycomb SCR catalyst. 2 performance methods and products. Background technique [0002] The promulgation of "Emission Standards of Air Pollutants for Thermal Power Plants (GB 13223-2011)" and "Action Plan for Energy Conservation and Emission Reduction Upgrading and Renovation of Coal Power Plants (2014-2020)" put forward new regulations on the emission limits of coal-fired power plants. demanding. NOx is one of the main pollutants emitted by coal-fired power plants. To meet the limit requirements of "ultra-clean emissions", efficient and stable flue gas denitrification must be achieved. At present, almost all large coal-fired power plants in my country have adopted selective catalytic reduction (SCR) technology as tail gas denitrification technology. Generally, the dosage of SCR cataly...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/88B01D53/90B01D53/56
CPCB01D53/8631B01D53/88B01D53/90
Inventor 张成李鑫李伟李权谭鹏余圣辉马仑陈刚方庆艳
Owner HUAZHONG UNIV OF SCI & TECH
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