Method for preparing SCR denitration catalyst at low temperatures

A technology of denitrification catalyst and low-temperature conditions, which is applied in chemical instruments and methods, physical/chemical process catalysts, separation methods, etc., can solve the problems of unproven catalytic activity, low denitrification efficiency, and unstable catalytic activity, etc., to achieve Good application prospect, low cost and low reaction temperature

Active Publication Date: 2019-07-26
CHINA PETROLEUM & CHEM CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Patent CN106807346A discloses a low-temperature denitrification catalyst, which loads Mg\Ca\Ba\Sr\Zn\Mn\Cu oxides on γ-Al2O3, and regulates the acidic active sites of the catalyst to prevent low-temperature hydration of activated alumina to make the catalyst both waterproof Combined with the ability to increase catalytic activity, the disadvantage of this catalyst is that there is no demonstration of the relationship between acidic sites and catalytic activity, so the catalytic activity is unstable and there are disadvantages such as high reaction temperature and difficult industrial application
[0005] To sum up, at present, the denitrification aids or catalysts developed by large companies at home and abroad generally use precious metals and the denitrification efficiency is not high. Researching a SCR low-temperature catalyst has important economic value and environmental protection value

Method used

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  • Method for preparing SCR denitration catalyst at low temperatures
  • Method for preparing SCR denitration catalyst at low temperatures
  • Method for preparing SCR denitration catalyst at low temperatures

Examples

Experimental program
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Effect test

Embodiment 1

[0031] (1) Preparation of molecular sieve carrier: first weigh 0.5mol 86g of titanium tetramethoxide (172) (titanium source) and dissolve it in absolute ethanol, stir it with a magnetic stirrer to mix it evenly, and adjust the pH of the aqueous solution of acetic acid to be 2, Then add 0.0263mol (10.08g) of yttrium nitrate hexahydrate (383.06) (precursor of rare earth metal) and 10g porogen (polyoxyethylene leaf amine) and stir (react at 60°C for 8h) to form a sol, evaporate ethanol and dry, 500 Roasting 12h obtains molecular sieve carrier TiO2-Y2O3, and the particle diameter of molecular sieve carrier is 0.2mm;

[0032] (2) Active component impregnation process: impregnate the molecular sieve carrier TiO2-Y2O3 (2h) with an aqueous solution of 1mol / L vanadic acid, and dry at room temperature to obtain a molecular sieve catalyst impregnated with vanadic acid;

[0033] (3) Roasting and oxidation process: put the impregnated molecular sieve catalyst in a muffle furnace and roast ...

Embodiment 2

[0035] (1) Preparation of molecular sieve carrier: first weigh 0.5mol 114g of tetraethoxytitanium (228) (titanium source) and dissolve it in absolute ethanol, stir it with a magnetic stirrer to mix it evenly, and adjust the pH with the aqueous solution of propionic acid After adding 0.01547mol (4.408g) of Sc(NO3)3·3H2O(285) (precursor of rare earth metal) and 10g of porogen (polyoxyethylene soybean amine) and stirring (reaction at 75°C for 5h) to form a sol, Dry after evaporating ethanol, and roast at 650°C for 10 hours to obtain molecular sieve carrier TiO2-Sc2O3, the particle size of molecular sieve is 0.6mm;

[0036] (2) Active component impregnation process: repeatedly impregnate the molecular sieve carrier TiO2-Sc2O3 (6h) with an aqueous solution of 1mol / L FeVO4, and dry at room temperature to obtain a molecular sieve catalyst impregnated with FeVO4;

[0037] (3) Roasting and oxidation process: put the impregnated molecular sieve catalyst in a muffle furnace and roast at ...

Embodiment 3

[0039] (1) Preparation of molecular sieve carrier: first weigh 0.5mol 170.2g of tetrapropoxytitanium (284.22) (titanium source) and dissolve it in absolute ethanol, stir it with a magnetic stirrer to mix it evenly, adjust the aqueous solution of propionic acid When the pH is 2, add 0.0005mol (0.2165) of La(NO3)·6H2O(433) (precursor of rare earth metal) and 10g of porogen (polyoxyethylene tallow amine) and stir (90°C for 2h) to form a sol, evaporate Dried with ethanol, roasted at 800°C for 8 hours to obtain molecular sieve carrier TiO2-La2O3, molecular sieve particle size is 1.0mm;

[0040] (4) Active component impregnation process: repeatedly impregnate the molecular sieve carrier TiO2-La2O3 (8h) with an aqueous solution of 1mol / L Mn(NO3)2, and dry at room temperature to obtain a molecular sieve catalyst impregnated with Mn(NO3)2;

[0041] (2) Roasting and oxidation process: put the impregnated molecular sieve catalyst in a muffle furnace and roast at 500°C to obtain the SCR d...

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Abstract

The invention relates to a method for preparing an SCR denitration catalyst at low temperatures. The method includes dissolving a titanium source in absolute ethyl alcohol, regulating the pH value to2-6 by an organic acid solution, adding a rare earth metal precursor, mixing a pore-forming agent, stirring to react at 60-90 DEG C for 2-8 hours, drying after the ethyl alcohol evaporates, and roasting at 500-800 DEG C for 8-12 hours so as to obtain a molecular sieve carrier; impregnating the molecular sieve carrier by one or more of a precursor metal salt of a transition metal oxide, an acid solution or a complex for 2-8 hours, and drying at a room temperature so as to obtain an impregnated molecular sieve catalyst of the precursor metal salt, the acid solution or the complex; roasting the impregnated molecular sieve catalyst in a muffle furnace for 500-800 DEG C so as to obtain the SCR denitration catalyst. When used in catalytic cracking flue gas, the catalyst is low in SCR denitrationreaction temperature, good in activity, high in conversion rate and long in service life, thereby having promising application prospect.

Description

technical field [0001] The invention belongs to the field of heterogeneous catalyst preparation, and relates to a preparation method of a catalyst for removing nitrogen oxides at low temperature. Background technique [0002] Environmental pollution caused by SOx and NOx emissions from catalytic cracking unit regeneration flue gas has attracted increasing attention. NOx is not only the main component of acid rain and photochemical smog, but also easily causes salt embrittlement and cracks in the downstream of the catalytic cracking regeneration system, resulting in damage. Safe production and sustainable development. Flue gas desulfurization technology has become increasingly mature and stable. For denitrification technology, the main FCC device flue gas deSOx technology, deNOx technology and desulfurization and denitrification integration technology, selective catalytic reduction (SCR) technology, ozone oxidation flue gas Denitrification technology, SNOx desulfurization an...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/22B01J23/28B01J23/30B01J23/34B01J23/63B01J23/83B01J23/847B01D53/86B01D53/56
CPCB01J23/22B01J23/8472B01J23/34B01J23/83B01J23/63B01J23/28B01J23/30B01D53/8628B01D2251/2062B01D2255/20707B01D2255/20723B01D2255/2061B01D2255/20738B01D2255/206B01D2255/2073B01D2255/20746B01D2255/20753B01D2255/1026B01D2255/1025B01D2255/2065B01D2255/1023B01D2255/20769B01D2255/20776B01D2255/1021
Inventor 赵耀崔蕊冯保杰钟广文于焕良
Owner CHINA PETROLEUM & CHEM CORP
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