Recovery and regeneration method of waste scr denitrification catalyst and regenerated scr catalyst carrier

A technology of SCR catalyst and catalyst, which is applied in the direction of catalyst regeneration/reactivation, chemical instruments and methods, physical/chemical process catalysts, etc. It can solve the problems of long route, complicated operation, short service life of catalyst, etc., and reduce the drying crack rate and wear rate, increase pore volume, and reduce production cost

Active Publication Date: 2016-05-18
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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  • Recovery and regeneration method of waste scr denitrification catalyst and regenerated scr catalyst carrier
  • Recovery and regeneration method of waste scr denitrification catalyst and regenerated scr catalyst carrier

Examples

Experimental program
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Effect test

Embodiment 1

[0043] Weigh 25 kg of waste catalyst, break it into small pieces of 0.5-1cm by a plastic crusher, pass through a 50-mesh vibrating sieve, add water to wash the dust, put the washed catalyst fragments into 60 kg of dilute nitric acid with a concentration of 1M and soak 1-2 hours, after filtration, wet pulverization by pulverizer, add 50 kg of water, control the concentration of catalyst slurry at 26wt%, put it into sand mill for ultrafine pulverization, and take samples to detect that the particle diameter is 20-50nm, which is qualified; unqualified two Second beating;

[0044] The qualified catalyst slurry and the metatitanic acid slurry are mixed according to the mass ratio of 1:1, and the TiO in the metatitanic acid slurry 2 The content is 190g / l, wash with water once for 1.5 hours, and then wash with water for the second time after press filtration. After washing for 3 hours, take a small amount of filtrate and test it with 1% red blood salt solution. When it turns yellow, ...

Embodiment 2

[0048] Weigh 25 kg of waste catalyst, break it into small pieces of 0.5-1cm by a plastic crusher, pass through a 50-mesh vibrating sieve, add water to wash the dust, put the washed catalyst fragments into 60 kg of dilute nitric acid with a concentration of 1M and soak 1-2 hours, after filtration, wet pulverization by pulverizer, add water to adjust the concentration of catalyst slurry to control at 30wt%, put it into sand mill for ultra-fine pulverization, and take samples to detect that the particle diameter is 50-100nm is qualified; unqualified secondary beating ;

[0049] The qualified catalyst slurry and the metatitanic acid slurry are mixed according to the mass ratio of 1:9, and the TiO in the metatitanic acid slurry 2 The content is 230g / l, wash with water once for 1.5 hours, and then wash with water for the second time after pressing for filtration. After washing for 3 hours, take a small amount of filtrate and test it with 1% red blood salt solution. When it turns yel...

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Abstract

The invention discloses a method for recovering and regenerating a waste SCR denitrification catalyst and a regenerated SCR catalyst carrier. The method for recovering and regenerating the waste SCR denitrification catalyst is to add the catalyst to the production process of metatitanic acid to produce titanium dioxide after preliminary treatment, remove the harmful components in the waste catalyst, and retain the active components in the catalyst, so as to obtain a It is a low-cost and environment-friendly recovery and regeneration method, and the performance effects of the regenerated catalyst carrier in all aspects can reach the standard for preparing SCR catalysts, and has excellent performance.

Description

technical field [0001] The invention belongs to the field of recovery and regeneration of denitrification catalysts, and in particular relates to a low-cost and environment-friendly recovery and regeneration method of waste SCR denitrification catalysts and a regenerated SCR catalyst carrier prepared therefrom. Background technique [0002] As the impact of PM2.5 on the environment becomes more and more serious, people pay more and more attention to factors such as smoke and automobile exhaust that produce PM2.5. More and more stringent, Selective Catalytic Reduction (SCR) denitrification technology is widely used in the denitrification system of coal-fired power plants due to its efficient and reliable denitrification performance. The principle of SCR denitrification technology is to inject NH into the exhaust gas of the boiler 3 These reducing agents react with the NOx in the flue gas under the action of the catalyst to generate harmless nitrogen and water. The core of S...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/30B01J38/00B01J38/48B01J38/60B01J38/02B01D53/56B01D53/86
Inventor 朱建兵李振兴
Owner PANZHIHUA ZHENGYUAN TECH
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