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Preparation method of highly active honeycomb SCR catalyst

A kind of SCR catalyst, honeycomb technology, which is applied in the field of preparation of highly active honeycomb SCR catalyst, can solve the problems of complex natural attapulgite composition, adverse effect on catalyst activity, and low activity of SCR catalyst, and achieve stable denitrification efficiency and enhanced denitrification Catalytic activity, wide range of effects

Active Publication Date: 2019-05-10
BEIJING GUODIAN LONGYUAN ENVIRONMENTAL ENG +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The technical problem to be solved is: the existing V 2 o 5 -WO 3 (MoO 3 ) / TiO 2 The cost of series catalysts is relatively high, and the composition of natural attapulgite is complex, which will have an adverse effect on the catalyst activity, and the SCR catalyst prepared from it as a raw material has low activity

Method used

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  • Preparation method of highly active honeycomb SCR catalyst
  • Preparation method of highly active honeycomb SCR catalyst

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Experimental program
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preparation Embodiment 1

[0030] Put the attapulgite in the nitric acid solution and stir for 1 hour, the mass volume ratio of the attapulgite to the nitric acid solution is 89:1; then filter, wash the attapulgite with desalted water, then roast and cool the attapulgite , the roasting temperature is 400°C, and the roasting time is 2h; after cooling to room temperature, it is ground and passed through a 200-mesh sieve to obtain activated attapulgite; Na in activated attapulgite 2 O content ≤ 0.2%, CaO content ≤ 0.5%, MgO content ≤ 1%; then mix the activated attapulgite with titanium dioxide, ammonium metavanadate, CMC, PEO, ammonia water, glass fiber, cotton pulp and desalted water evenly Mixing is carried out, wherein the volume percentage of ammonia water used is 30%; the mud after mixing is pre-extruded and filtered with a vacuum screw extruder and a steel wire filter, and the extruded material is aged at room temperature for 24 hours; the aged mud is used Extruded by a screw extruder to make a catal...

preparation Embodiment 2

[0032] Put the attapulgite in the nitric acid solution and stir for 2 hours, the mass volume ratio of the attapulgite to the nitric acid solution is 89:1; then filter, wash the attapulgite with desalted water, then roast and cool the attapulgite , the roasting temperature is 200°C, and the roasting time is 4h; after cooling to room temperature, it is ground and passed through a 200-mesh sieve to obtain activated attapulgite; Na in activated attapulgite 2 O content ≤ 0.2%, CaO content ≤ 0.5%, MgO content ≤ 1%; then mix the activated attapulgite with titanium dioxide, ammonium metavanadate, CMC, PEO, ammonia water, glass fiber, cotton pulp and desalted water evenly Mixing is carried out, wherein the volume percentage of ammonia water used is 30%; the mud after mixing is pre-extruded and filtered with a vacuum screw extruder and a steel wire filter, and the extruded material is aged at room temperature for 12 hours; the aged mud is used Extruded by a screw extruder to make a cata...

preparation Embodiment 3

[0034]Put the attapulgite in the nitric acid solution and stir for 1.5h, the mass volume ratio of the attapulgite to the nitric acid solution is 89:1; then filter, wash the attapulgite with demineralized water, and then roast the attapulgite and Cooling, roasting temperature is 300 ℃, roasting time is 2h; after cooling to room temperature, grind, and pass through a 600 mesh sieve to obtain activated attapulgite; Na in activated attapulgite 2 O content ≤ 0.2%, CaO content ≤ 0.5%, MgO content ≤ 1%; then mix the activated attapulgite with titanium dioxide, ammonium metavanadate, CMC, PEO, ammonia water, glass fiber, cotton pulp and desalted water evenly Mixing is carried out, wherein the volume percentage of ammonia water used is 30%; the mud after mixing is pre-extruded and filtered by a vacuum screw extruder and a steel wire filter, and the extruded material is aged at room temperature for 20 hours; the aged mud is used Extruded by a screw extruder to make a catalyst green body...

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Abstract

The invention relates to the technical field of SCR catalysts and discloses a high-activity honeycomb SCR catalyst and a preparation method thereof. The invention includes the following raw material components in parts by weight: 188-376 parts of attapulgite, 1000 parts of titanium dioxide, 10.1-14.4 parts of ammonium metavanadate, 2.1-4.2 parts of sodium carboxymethylcellulose, and polyethylene oxide 6‑10 parts, 85 parts ammonia, 63‑70 parts glass fiber, 6.1‑10.2 parts cotton pulp, 2820 parts nitric acid solution and 470‑530 parts desalted water. The invention has low cost, simple preparation process and easy operation, and high catalytic activity.

Description

technical field [0001] The invention relates to the technical field of SCR catalysts, in particular to a preparation method of a highly active honeycomb SCR catalyst. Background technique [0002] NO X It is one of the main pollutants in the atmosphere, which can cause the greenhouse effect, acid rain, photochemical smog and the destruction of the ozone layer. The flue gas released by burning coal is NO X The main source, the flue gas contains a large amount of NO, NO 2 and a small amount of N 2 O, control NO X Emissions are of great significance to environmental protection. At present, the most widely used and mature flue gas denitrification technology in coal-fired power plants is the selective catalytic reduction method, and its core technology is the SCR denitrification catalyst. The most widely used SCR denitration catalyst in industry is V 2 o 5 -WO 3 (MoO 3 ) / TiO 2 A series of catalysts, in which the carrier TiO 2 accounting for the vast majority. But TiO...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/30B01J35/04B01D53/86B01D53/90B01D53/56
CPCB01D53/8628B01D53/90B01J23/002B01J23/30B01D2255/802B01D2258/0283B01J2523/00B01J35/39B01J35/56B01J2523/47B01J2523/55B01J2523/68B01J2523/69
Inventor 周凤翔肖雨亭白伟陆金丰徐光辉
Owner BEIJING GUODIAN LONGYUAN ENVIRONMENTAL ENG