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Low cost recovery and regeneration method of waste SCR catalyst, and regenerated SCR catalyst carrier

A kind of SCR catalyst and catalyst technology, which is applied in the field of regenerated SCR catalyst carrier, can solve the problems of long route, short service life of catalyst, complicated operation, etc., and achieve the effect of reducing dry crack rate and wear rate, reducing production cost and increasing pore volume

Active Publication Date: 2015-02-25
PANZHIHUA ZHENGYUAN TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The patent application with the application number CN201210492800.0 discloses a recycling and regeneration method for waste SCR catalysts. This method is only after soot blowing and ball milling, adding active substances such as metal oxides to make catalysts, in which harmful substances such as sodium, potassium and other ions cannot be removed, and ball milling cannot reach the effective particle diameter, resulting in a short service life of the catalyst made by this method, and a rapid reduction in catalytic ability; and the present invention effectively solves the above problems
[0007] The patent application with the application number CN201310434204.1 discloses a recovery and regeneration method for waste SCR catalysts. There are three methods for this method: 1. Completely separate the components of the catalyst to re-obtain separate titanium dioxide, tungsten trioxide and other substances , the route is lengthy, the operation is complicated, the cost is high, and the economic value is low; 2 is on-line regeneration through soot blowing, drying, etc., the regenerated catalyst has low activity recovery ability, and it can only be used for catalysts that are only blocked but not poisoned; 3 is the production of rutile In the regeneration process of pigment titanium dioxide, the waste SCR catalyst is crushed to about 300 mesh (about 44 μm), and then the product is obtained through pickling, water washing, pressure filtration, concentration, hydrolysis, suction filtration, bleaching, calcination, etc.; but the rutile titanium dioxide Can only be used on pigments, not as a carrier for SCR catalysts

Method used

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  • Low cost recovery and regeneration method of waste SCR catalyst, and regenerated SCR catalyst carrier
  • Low cost recovery and regeneration method of waste SCR catalyst, and regenerated SCR catalyst carrier

Examples

Experimental program
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Embodiment 1

[0037] Weigh 25 kg of waste catalyst, crush it into small fragments of 0.5-1 cm by a plastic crusher, pass through a 50-mesh vibrating sieve, and add water to wash the dust, and put the washed catalyst fragments into 60 kg of 1M diluted nitric acid to soak. 1-2 hours, after filtration, wet pulverization by a pulverizer, add 50 kg of water, the concentration of the catalyst slurry is controlled at 26wt%, go into a sand mill for ultrafine pulverization, and the particle diameter of 20-55nm is qualified by sampling; secondary beating;

[0038] Catalyst slurry and TiO with qualified particle size 2 The metatitanic acid slurry with a content of 26wt% is mixed according to the mass ratio of 1:1, pure water is added until titanium dioxide accounts for about 23wt% of the total slurry, ammonia water is added to adjust the pH to 7.5, and ammonium paratungstate and white carbon black are added. , the addition amount respectively meets the following requirements: WO 3 The content accoun...

Embodiment 2

[0041] Weigh 25 kg of waste catalyst, crush it into small fragments of 0.5-1 cm by a plastic crusher, pass through a 50-mesh vibrating sieve, and add water to wash the dust, and put the washed catalyst fragments into 60 kg of 1M diluted nitric acid to soak. 1-2 hours, after filtration, wet pulverization by a pulverizer, adding water to adjust the concentration of the catalyst slurry to 30wt%, and entering into a sand mill for ultra-fine pulverization, sampling and testing particle diameters of 50-100nm are qualified; unqualified secondary beating;

[0042] Combine the above-mentioned catalyst slurry with qualified particle size with TiO 2 The metatitanic acid slurry with a content of 30wt% is mixed according to the mass ratio of 1:9, pure water is added until titanium dioxide accounts for about 23wt% of the total slurry, ammonia water is added to adjust the pH to 8.0, and ammonium paratungstate and white carbon black are added. , the addition amount respectively meets the fol...

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Abstract

The present invention discloses a low cost recovery and regeneration method of a waste SCR catalyst, and a regenerated SCR catalyst carrier. According to the low cost recovery and regeneration method of the waste SCR catalyst, a catalyst is subjected to a primary treatment and then is mixed with a metatitanic acid slurry to co-prepare titanium-tungsten powder, harmful components in the waste catalyst are removed, and the active ingredients in the catalyst are retained so as to obtain the low cost and environmental protection recovery and regeneration method. In addition, various performance effects of the regenerated SCR catalyst carrier can achieve the standard for preparing the SCR catalyst, and the excellent performance is provided.

Description

technical field [0001] The invention belongs to the field of recovery and regeneration of denitration catalysts, and in particular relates to a low-cost recovery and regeneration method for waste SCR denitration catalysts and a regenerated SCR catalyst carrier prepared therefrom. Background technique [0002] As the impact of PM 2.5 on the environment is becoming more and more serious, people are paying more and more attention to factors such as flue gas and vehicle exhaust that generate PM 2.5. Since the 12th Five-Year Plan, my country's control of nitrogen oxide (NOx) emissions has become The more stringent, selective catalytic reduction (SCR) denitration technology is widely used in the denitration system of coal-fired power plants because of its efficient and reliable denitration performance. The principle of SCR denitration technology is to inject NH into the flue gas discharged from the boiler. 3 and other reducing agents, these reducing agents react with NOx in the fl...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/92B01J38/00B01J32/00
Inventor 朱建兵李振兴
Owner PANZHIHUA ZHENGYUAN TECH
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