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Low-temperature selective catalytic reduction denitration catalyst and preparation method thereof

A denitration catalyst and selective technology, applied in the direction of catalyst activation/preparation, physical/chemical process catalyst, chemical instruments and methods, etc., can solve the problems of difficult control of catalyst preparation conditions, serious high temperature ablation of activated carbon, and high cost of catalytic preparation, To achieve the effect of improving denitration activity and efficiency, large adsorption capacity, and improving catalytic performance

Active Publication Date: 2010-03-03
ANHUI WEIDA ENVIRONMENTAL PROTECTION TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantages are: first, the cost of catalytic preparation is high, and the toxicity is strong; second, the catalyst preparation conditions are relatively strict and difficult to control; third, the operating temperature is high at 350-400 ° C, and the control is strict, which is not suitable for the existing power plants in my country. The actual situation that the temperature is low after gas desulfurization and dust removal; the fourth is V 2 o 5 for SO 2 Oxidation to SO 3 The reaction is catalytic, and the resulting SO 3 with escaped NH 3 React with water vapor in the flue gas to form NH 4 HSO 4 , below its dew point (300-330°C), it condenses on equipment and pipelines causing blockage and corrosion
The advantage of the catalyst prepared with activated carbon as the carrier is that the rich specific surface area of ​​the activated carbon carrier is conducive to the dispersion of the active components, and it has a certain anti-SO2 performance, but the activated carbon is ablated at high temperature during the activation and regeneration process. Too serious, resulting in excessive catalyst loss

Method used

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  • Low-temperature selective catalytic reduction denitration catalyst and preparation method thereof
  • Low-temperature selective catalytic reduction denitration catalyst and preparation method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0017] Store and homogenize the attapulgite clay ore in advance;

[0018] Add the piled attapulgite clay to the water for stirring. The mass percentage of the attapulgite clay and water is 65%: 35%. Then the evenly stirred attapulgite clay is cut by a pair of rollers and a multi-roll extruder. Cut and extrude attapulgite clay flakes to promote the depolymerization and dispersion of attapulgite crystal bundles;

[0019] Dry the attapulgite clay flakes, and then pulverize them into attapulgite clay powder passing through a 200-mesh sieve;

[0020] Add 100g of attapulgite clay powder into 2L of water, age for 10h, stir at high speed for 20min to make the attapulgite clay powder into a uniform slurry, and then add 50mL of sulfuric acid with a mass concentration of 10% and 100mL with a concentration of 100g / L manganese nitrate solution, keep stirring for 30 minutes to obtain a suspension, and then slowly add 4mol / L sodium hydroxide solution until the pH value of the suspension is 8-10, ...

Embodiment 2

[0024] Store and homogenize the attapulgite clay ore in advance;

[0025] Add the piled attapulgite clay to the water for stirring. The mass percentage of the attapulgite clay and water is 65%: 35%. Then the evenly stirred attapulgite clay is cut by a pair of rollers and a multi-roll extruder. Cut and extrude attapulgite clay flakes to promote the depolymerization and dispersion of attapulgite crystal bundles;

[0026] Dry the attapulgite clay flakes, and then pulverize them into attapulgite clay powder passing through a 200-mesh sieve;

[0027] Add 100g of attapulgite clay powder into 2L of water, age for 10h, stir at high speed for 20min to make the attapulgite clay powder into a uniform slurry, and then add 50mL sulfuric acid with a mass concentration of 10% and 200mL with a concentration of 10g / L of copper nitrate and 100mL of 100g / L manganese nitrate solution, continue to stir for 30min to obtain a suspension, then slowly add 4mol / L of sodium hydroxide solution until the pH of...

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Abstract

The invention discloses a low-temperature selective catalytic reduction denitration catalyst and a preparation method thereof, wherein the catalyst takes an attapulgite as a carrier to load nano-composite materials of manganese oxide nano-particles; the structure thereof is as follows: manganese oxide particles with the particle diameter of less than 20nm are loaded on the rod-shaped crystal surface of the attapulgite with the diameter of 40-50nm; one or more types from iron, copper and nickel are added as an additive; and calculated according to the mass percentage of manganese, the content of the manganese oxide in the catalyst is 0.1-20. The preparation method comprises the steps of: firstly extruding, drying and crushing the attapulgite clay, and then preparing attapulgite clay powderinto suspension liquid; adding acid solution to wash and remove carbonate impurities, adding manganese salt, and then adding alkali solution for stirring so as to lead the manganese ion to be hydrolyzed and precipitated and loaded onto the crystal surface of the attapulgite, and finally obtaining the product after centrifugal washing, dewatering, drying and calcinations. The catalyst takes ammoniaas a reducing agent, and has higher activity of catalyzing NH3 and reducing NO reaction within the scope of 120 DEG C to 350 DEG C.

Description

Technical field [0001] The invention relates to the field of air pollution control engineering, in particular to a low-temperature selective catalytic reduction denitration catalyst and a preparation method thereof. Background technique [0002] Thermal power plants produce large amounts of CO during high-temperature combustion 2 , SO 2 , NOx, to cause acid rain in 81.6% of the cities across the country. The emission of nitrogen oxides can also cause regional environmental pollution problems such as photochemical smog and ozone layer destruction. As a large-scale NOx emission point pollution source, thermal power plants have become the main source of NOx pollution control. Currently, there are two main types of technologies for reducing nitrogen oxides in power plants: The first type is combustion process control, that is, improving combustion methods to reduce the generation of nitrogen oxides during the combustion process (including low-oxygen combustion technology, multi-end ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/34B01J21/16B01J23/889B01J37/00B01J37/03B01D53/56B01D53/86
Inventor 陈天虎李金虎张先龙刘海波陈冬
Owner ANHUI WEIDA ENVIRONMENTAL PROTECTION TECH
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