A kind of preparation method for scr denitrification catalyst under low temperature condition

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 no correlation of catalytic activity, difficulty in industrial application, and low denitrification efficiency, and achieve the goal of overcoming low temperature The effect of low activity and instability, promotion of uniform loading, and good application prospects

Active Publication Date: 2022-06-21
CHINA PETROLEUM & CHEM CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

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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  • A kind of preparation method for scr denitrification catalyst under low temperature condition
  • A kind of preparation method for scr denitrification catalyst under low temperature condition
  • A kind of preparation method for scr denitrification catalyst under low temperature condition

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Experimental program
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Effect test

Embodiment 1

[0031] (1) preparation of molecular sieve carrier: at first weigh 0.5mol 86g of titanium tetramethoxide (172) (titanium source) to be dissolved in dehydrated alcohol, stir with a magnetic stirrer to make it evenly mixed, and the aqueous solution of acetic acid is adjusted to pH 2, Then, 0.0263mol (10.08g) of yttrium nitrate hexahydrate (383.06) (precursor of rare earth metal) and 10g of porogen (polyoxyethylene leafamine) were added and stirred (reaction at 60°C for 8h) to form a sol, evaporated ethanol and dried at 500 After roasting for 12h, the molecular sieve carrier TiO2-Y2O3 was obtained, and the particle size of the molecular sieve carrier was 0.2 mm;

[0032] (2) Impregnation process of active components: impregnating molecular sieve carrier TiO2-Y2O3 with an aqueous solution of 1 mol / L vanadic acid (2h), and drying at room temperature to obtain a molecular sieve catalyst impregnated with vanadic acid;

[0033] (3) Roasting and oxidation process: the impregnated molecu...

Embodiment 2

[0035] (1) Preparation of molecular sieve carrier: firstly, 0.5mol 114g of tetraethoxytitanium (228) (titanium source) was weighed and dissolved in absolute ethanol, stirred with a magnetic stirrer to make it evenly mixed, and the aqueous solution of propionic acid was adjusted to pH is 2, then 0.01547mol (4.408g) of Sc(NO3)3·3H2O(285) (precursor of rare earth metal) and 10g of porogen (polyoxyethylene soybean amine) were added and stirred (reaction at 75°C for 5h) to form a sol, After evaporating ethanol, drying, calcining at 650°C for 10h to obtain molecular sieve carrier TiO2-Sc2O3, molecular sieve particle size is 0.6mm;

[0036] (2) Impregnation process of active components: The molecular sieve carrier TiO2-Sc2O3 is repeatedly impregnated with an aqueous solution of 1 mol / L FeVO4 (6h), and dried at room temperature to obtain a molecular sieve catalyst impregnated with FeVO4;

[0037] (3) Roasting and oxidation process: the impregnated molecular sieve catalyst was roasted ...

Embodiment 3

[0039] (1) Preparation of molecular sieve carrier: firstly, 0.5mol 170.2g of tetrapropoxide titanium (284.22) (titanium source) was weighed and dissolved in absolute ethanol, stirred with a magnetic stirrer to make it evenly mixed, and the aqueous solution of propionic acid was adjusted The pH was set to 2, then 0.0005mol (0.2165) of La(NO3)·6H2O(433) (precursor of rare earth metal) and 10g of porogen (polyoxyethylene tallowamine) were added and stirred (reaction at 90°C for 2h) to form a sol, which was evaporated After drying with ethanol, calcined at 800°C for 8h to obtain the molecular sieve carrier TiO2-La2O3, and the molecular sieve particle size is 1.0mm;

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

[0041] (2) Roasting and oxidation process: the impreg...

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Abstract

The invention belongs to a preparation method for an SCR denitration catalyst under low temperature conditions. Dissolve titanium source in absolute ethanol, adjust pH to 2-6 with organic acid solution, add rare earth metal precursor and porogen, mix and stir, react at 60-90°C for 2-8h, evaporate ethanol and dry, 500- Roast at 800°C for 8-12 hours to obtain a molecular sieve carrier; impregnate the molecular sieve carrier with one or more of transition metal oxide precursor metal salts or acid solutions or complexes, impregnate for 2-8 hours, and dry at room temperature to obtain an impregnated precursor Molecular sieve catalysts of metal salts or acid solutions or complexes; the impregnated molecular sieve catalysts are roasted in a muffle furnace at 500-800°C to obtain SCR denitration catalysts. The catalyst of the invention is used for SCR denitrification reaction temperature in catalytic cracking flue gas, has low temperature, good activity, high conversion rate, long service life and good 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] The pollution to the environment caused by the emission of SOx and NOx from the regenerated flue gas of catalytic cracking units has been paid more and more attention. NOx is not only the main component of acid rain and photochemical smog, but also easily causes nitrite embrittlement and cracks in the downstream of the catalytic cracking regeneration system, resulting in damage. Safe production and sustainable development. The flue gas desulfurization technology has become increasingly mature and stable, and for the denitrification technology, the existing main FCC units are flue gas desulfurization technology, deNOx technology and integrated desulfurization and denitrification technology, selective catalytic reduction (SCR) technology, ozone oxidation ...

Claims

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Application Information

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Patent Type & Authority Patents(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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