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Composite smoke SCR (selective catalytic reduction) denitrification catalyst and preparation method thereof

A composite catalyst and catalyst technology, applied in molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of difficult to achieve industrial production, difficult to deal with deactivated catalysts, and high catalyst preparation costs, and reach the active temperature. The effect of wide window, strong resistance to SO2 and H2O poisoning, and high SCR denitration efficiency

Active Publication Date: 2013-03-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among the patents on low-temperature flue gas denitration catalysts and their preparation in the prior art, the catalysts disclosed in patents CN 101428215A, CN 10134722A, CN 101468314A, CN 101422728A and CN 101676019A all contain toxic components such as vanadium and tungsten, which seriously pollute the environment. The deactivated catalyst is difficult to handle; and the catalyst temperature above 180°C can achieve 90% denitrification rate
The catalyst disclosed in the patent CN 10554581A uses precious metals as active components, which is expensive, and the conversion rate of nitrogen monoxide of the catalyst is over 60% at 250°C
The catalysts disclosed in patents such as CN 101069855A, CN 101428215A, and CN 101658787A use mesoporous molecular sieve as a carrier or nano-scale titanium dioxide as a carrier. The disadvantages are that the catalyst has high preparation cost, complex process, and is difficult to realize industrial production.

Method used

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  • Composite smoke SCR (selective catalytic reduction) denitrification catalyst and preparation method thereof
  • Composite smoke SCR (selective catalytic reduction) denitrification catalyst and preparation method thereof
  • Composite smoke SCR (selective catalytic reduction) denitrification catalyst and preparation method thereof

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Effect test

Embodiment 1

[0030] Prepare flue gas SCR denitrification composite catalyst according to the method of the present invention, the preparation method is:

[0031] (1) Place the honeycomb ceramic carrier in an ultrasonic oscillator, pour in deionized water for ultrasonic cleaning, and then dry it. Continue to immerse the above dedusted carrier in 5% nitric acid solution and boil for 8 hours. After cooling, clean the surface layer of the carrier and the residual acid in the pores with deionized water, and then dry it for later use.

[0032] (2) Weigh the precursors of catalyst active components: manganese acetate, molybdenum nitrate and nickel nitrate according to the molar ratio of Mn / Mo / Ni 1:0.1:0.2, mix and dissolve them in 15ml of deionized water, and stir well A certain amount of co-catalyst precursor cerium nitrate is added to the solution to prepare a saturated solution, wherein the molar ratio of Mn element to co-catalyst precursor is 1:0.2.

[0033] (3) Immerse the honeycomb ceramic...

Embodiment 2

[0049] Prepare flue gas SCR denitrification composite catalyst according to the method of the present invention, the preparation method is:

[0050] (1) Put the molecular sieve carrier into an ultrasonic oscillator, pour in deionized water for ultrasonic cleaning, and then dry it. Continue to immerse the above dedusted carrier in 14% citric acid solution and boil for 9 hours. After cooling, clean the surface layer of the carrier and the residual acid in the pores with deionized water, and then dry it for later use.

[0051] (2) Weigh the catalyst active component precursors: manganese chloride, molybdenum chloride and nickel nitrate according to the molar ratio of Mn / Mo / Ni element 1:0.3:0.1, mix and dissolve them in 20ml of deionized water, stir well After uniformity, add a certain amount of co-catalyst precursor copper nitrate and cerium acetate to the solution to obtain a saturated solution, wherein the molar ratio of Cu / Ce is 2:1, and the molar ratio of Mn element to co-cat...

Embodiment 3

[0057] Prepare flue gas SCR denitrification composite catalyst according to the method of the present invention, the preparation method is:

[0058] (1) Put the activated carbon carrier into an ultrasonic oscillator, pour in deionized water for ultrasonic cleaning, and then dry it. Continue to immerse the above dedusted carrier in 26% carbonic acid solution and boil for 10 hours. After cooling, clean the surface layer of the carrier and the residual acid in the pores with deionized water, and then dry it for later use.

[0059] (2) Weigh the precursors of catalyst active components: manganese nitrate, molybdenum chloride and nickel nitrate according to the molar ratio of Mn / Mo / Ni elements 1:0.4:0.9, mix and dissolve them in 17ml deionized water, and stir well Finally, add a certain amount of co-catalyst precursor chromium chloride and cerium chloride in the solution to obtain a saturated solution, wherein the element molar ratio of Cr / Ce is 1:1, and the molar ratio of Mn eleme...

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Abstract

The invention relates to a composite smoke SCR (selective catalytic reduction) denitrification catalyst. The composite smoke SCR denitrification catalyst takes honeycomb ceramics, activated carbon or a molecular sieve as a carrier. A composite manganese-molybdenum-nickel-loaded metal oxide is an active component, one or more of copper, chromium, cerium, tin and lanthanum are used as cocatalysts, and the total mass of the active components of the catalyst and the cocatalysts accounts for 15-30% of the mass of the carrier, wherein the molar ratio of Mn to Mo to Ni is 1:(0.1-1):(0.1-1), and the molar ratio of manganese to a metallic element of the co-catalyst is 1: (0.1-1). The catalyst provided by the invention is prepared by adopting a dipping method. Compared with the existing denitrification catalyst suitable for the temperature lower than 300 DEG C, the catalyst provided by the invention has the advantages of high denitrification efficiency, low cost, simple production process, long service life, wide active temperature window, high SO2 and H2O poison resistance capability and the like. Within the temperature from 80 DEG C to 300 DEG C, the conversion rate of NO is more than 90%.

Description

technical field [0001] The invention relates to a flue gas denitration catalyst and a preparation method thereof, in particular to a selective catalytic reduction (SCR) denitration composite catalyst and a preparation method thereof, belonging to the fields of air pollution control technology and environmental protection catalytic materials. Background technique [0002] Nitrogen oxides are one of the main pollutants in the atmospheric environment. Atmospheric NO X It can cause acid rain, photochemical smog, surface water eutrophication and other problems that damage the ecological environment and endanger human health. With NO X Emissions continue to increase, and environmental pollution is becoming more and more serious. my country has promulgated and implemented emission standards for air pollutants from thermal power plants for four times. The latest standard promulgated in 2009 stipulates that coal-fired power plants newly built, rebuilt and expanded in key areas sha...

Claims

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Application Information

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IPC IPC(8): B01J23/889B01J29/00B01J35/10B01D53/56B01D53/86
Inventor 祝社民卫平波童志武樊恩亚沈岳松沙志强张舒杨沈树宝徐凌
Owner CHINA PETROLEUM & CHEM CORP
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