High-temperature iron-based zeolite molecular sieve honeycomb type denitration catalyst and preparation method thereof

A technology of denitrification catalyst and iron-based zeolite, which is applied in the field of high-temperature iron-based zeolite molecular sieve honeycomb denitrification catalyst and its preparation, to achieve the effects of simplifying the production process, reducing production cost and low price

Active Publication Date: 2017-12-29
VALIANT CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

This patented technology allows for better control over the addition of various chemical agents during synthesis compared to previous methods like adding different types of reagents separately beforehand. It also extends the shelf life of these materials due to their stable structure even after being mixed together. Overall, this new method provides an efficient way to produce highly effective NOx reduction catalyzer (NO2/N) without requiring expensive equipment such as Vanadium Titanum Transistor).

Problems solved by technology

Technical Problem addressed in this patented text relates to improving the properties of NOX removal catalysis systems without causing damage caused by harmful gases like mercurialdecyttrium(V2) hexaferrite). Current commercially available catalyst carriers suffer severe degradations when exposed to these harsh environments during manufacturing processes. To solve this problem, research efforts were focused towards developing new types of catalysitive materials containing no transition elements called manganes, tantalites, bismuth compounds, and silicon oxynthanozirconiums.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0052] (1) dry mix

[0053] Add 226.7g ferrous chloride tetrahydrate (the mass is 144.7g in terms of ferrous chloride), 15.5g ferric chloride hexahydrate (the mass is 9.3g in terms of ferric chloride), 210.0g SSZ- 39 synthetic zeolite molecular sieves (SiO 2 with Al 2 o 3 The molar ratio is 15.5:1), 1078.0g natural zeolite molecular sieve powder, 1078.0g attapulgite clay, 67.2g amino carboxymethyl cellulose, 16.8g polyethylene oxide and 14.0g stearic acid for dry mixing, dry mixing stirring speed Be 300 revs / min, the time is 20min, obtains mixed dry material;

[0054] (2) Primary mixing

[0055] Add 1673.8g deionized water (the water of crystallization in ferrous chloride tetrahydrate and ferric chloride hexahydrate is negligible in the mixed dry material of gained in step (1), take the quality of ferrous chloride and ferric chloride as benchmark Calculate the water consumption) for stirring and mixing, the stirring speed is 750 rpm, until the temperature of the mud in th...

Embodiment 2

[0070] (1) dry mix

[0071] Add 326.3g ferrous acetate tetrahydrate (quality is 230.8g in terms of ferrous acetate), 21.2g iron sulfate, 252.0g SSZ-16 synthetic zeolite molecular sieve (SiO 2 with Al 2 o 3 The mol ratio is 25:1), 1568.0g natural zeolite molecular sieve powder, 392.0g attapulgite clay, 78.4g amino carboxymethyl cellulose and 8.4g stearic acid are dry mixed, and the dry mixed stirring speed is 350 rpm, The time is 25min, and the mixed dry material is obtained;

[0072] (2) Primary mixing

[0073] Add 1924.3g deionized water (the water of crystallization in ferrous acetate tetrahydrate is negligible in the mixed dry material of gained in step (1), calculate water consumption based on the quality of ferrous acetate) and stir and mix, stirring speed is 700 rpm until the temperature of the mud in the mixer reaches 80-90°C, and the mixing time of the material within this temperature range is 2 hours;

[0074] (3) Secondary mixing

[0075]After the primary mixin...

Embodiment 3

[0088] (1) dry mix

[0089] Add 176.5g ferrous nitrate hexahydrate (the quality is 110.3g in terms of ferrous nitrate) in the mixer, 49.6g iron nitrate nonahydrate (the quality is 29.7g in terms of ferric nitrate), 420.0g Zeolite Beta synthetic zeolite molecular sieve ( The molar ratio of SiO2 and Al2O3 is 50:1), 938.0g natural zeolite molecular sieve powder, 938.0g kaolin, 25.2g hydroxypropyl methylcellulose, 50.4g polyethylene oxide and 11.2g stearic acid are dry mixed, dry mixed The stirring speed is 400 rev / min, and the time is 22min to obtain the mixed dry material;

[0090] (2) Primary mixing

[0091] Add 1546.2g deionized water (the water of crystallization in ferrous nitrate hexahydrate and ferric nitrate nonahydrate is ignored in the mixed dry material of gained in step (1), calculate water consumption with the quality of ferrous nitrate and ferric nitrate) Stir and mix at a stirring speed of 800 rpm until the temperature of the mud in the mixer reaches 80-90°C, and...

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Abstract

The invention relates to a high-temperature iron-based zeolite molecular sieve honeycomb type denitration catalyst and a preparation method thereof, and belongs to the technical field of atmospheric pollution treatment technologies and environmentally friendly catalyzing materials. The preparation method comprises the following steps: mixing ferrous salts with ferrite; synthesizing a zeolite molecular sieve, natural zeolite molecular sieve powder, attapulgite clay or kaolin, glass fibers, an organic binding agent, wood pulp or sesbania cannabina powder, stearic acid and glycerinum; and carrying out mixing, ageing, extrusion forming, drying and roasting to obtain the iron-based zeolite molecular sieve honeycomb type denitration catalyst. According to the catalyst, the zeolite molecular sieve and natural raw mineral materials which have excellent thermal stability are used as carriers, and the running stability, the sintering resistance and the mechanical strength of the catalyst in a high-temperature environment are improved. The obtained honeycomb type denitration catalyst has good water resistance and sulfur poisoning resistance, and the conversion ratio of oxynitride is greater than 90% under the conditions that the temperature is in the high-temperature range of 400-600 DEG C and the air speed is 10,000 h<-1>.

Description

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Claims

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Application Information

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Owner VALIANT CO LTD
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