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SCR denitration catalyst applicable to glass melter smoke and preparing method of SCR denitration catalyst

A denitration catalyst, glass melting furnace technology, applied in chemical instruments and methods, heterogeneous catalyst chemical elements, physical/chemical process catalysts, etc., can solve the problems of high cost, short life, low catalyst denitration efficiency, etc. Simple method and evenly distributed effect

Inactive Publication Date: 2017-05-31
GLASS TECH RES INST OF SHAHE CITY OF HEBEI PROVINCE
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] At present, most of the denitrification equipment used in domestic glass melting furnaces are denitrification equipment of coal-fired power plants, and most of the catalysts used are imported from abroad. Not only is the cost high, but also such catalysts are prone to produce alkali in the special environment of glass melting furnace flue gas. The phenomenon of metal poisoning makes the denitrification efficiency of the catalyst low and the service life short

Method used

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  • SCR denitration catalyst applicable to glass melter smoke and preparing method of SCR denitration catalyst
  • SCR denitration catalyst applicable to glass melter smoke and preparing method of SCR denitration catalyst
  • SCR denitration catalyst applicable to glass melter smoke and preparing method of SCR denitration catalyst

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Experimental program
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Effect test

Embodiment 1

[0026] 1) Weigh raw materials

[0027] The raw material components are calculated by mass percentage: 68.99% of titanium dioxide; 1.14% of ammonium metavanadate; 7.74% of ammonium tungstate; 8.38% of cerium nitrate; 8.68% of ammonium molybdate;

[0028] 2) Stir and dissolve ammonium tungstate + oxalic acid in deionized water, stir and add titanium dioxide after complete dissolution, stir magnetically for 2 hours, then heat and stir in a water bath to evaporate to dryness, put it in an oven to evaporate to dryness at 100 degrees Celsius, calcine at 450 degrees Celsius for 4 hours, and cool naturally. Grind through an 80-mesh sieve as a powder; stir and dissolve cerium nitrate + ammonium molybdate + ammonium metavanadate + oxalic acid in deionized water, stir and add the powder after complete dissolution, stir magnetically for 2 hours, then heat and evaporate in a water bath, and put it in an oven Evaporate to dryness at 100°C, calcinate at 450°C for 4 hours, cool naturally, and...

Embodiment 2

[0035] 1) Weigh raw materials

[0036] The raw material components are as follows according to mass percentage: 62.06% of titanium dioxide; 1.02% of ammonium metavanadate; 6.96% of ammonium tungstate; 7.54% of cerium nitrate; 7.81% of ammonium molybdate;

[0037] 2) Stir and dissolve ammonium tungstate + oxalic acid in deionized water, stir and add titanium dioxide after complete dissolution, stir magnetically for 3 hours, then heat and stir in a water bath to evaporate to dryness, put it in an oven to evaporate to dryness at 80 degrees Celsius, calcine at 500 degrees Celsius for 5 hours, and cool naturally. Grind through a 100-mesh sieve as a powder; stir and dissolve cerium nitrate + ammonium molybdate + ammonium metavanadate + oxalic acid in deionized water, stir and add powder after complete dissolution, magnetically stir for 3 hours, then heat and evaporate in a water bath, and put it in an oven Evaporate to dryness at 80°C, calcinate at 500°C for 5 hours, cool naturally,...

Embodiment 3

[0044] 1) Weigh raw materials

[0045] The raw material components are as follows according to mass percentage: 63.08% of titanium dioxide; 1.44% of ammonium metavanadate; 7.86% of ammonium tungstate; 7.69% of cerium nitrate; 5.20% of ammonium molybdate;

[0046]2) Stir and dissolve ammonium tungstate + oxalic acid in deionized water, stir and add titanium dioxide after complete dissolution, stir magnetically for 4 hours, then heat and stir in a water bath to evaporate to dryness, put it in an oven to evaporate to dryness at 90 degrees Celsius, calcine at 550 degrees Celsius for 6 hours, and cool naturally. Grind through a 120-mesh sieve as a powder; stir and dissolve cerium nitrate + ammonium molybdate + ammonium metavanadate + oxalic acid in deionized water, stir and add powder after complete dissolution, magnetically stir for 4 hours, then heat in a water bath and evaporate to dryness, put in an oven Evaporate to dryness at 90°C, calcinate at 550°C for 6 hours, cool natural...

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Abstract

The invention discloses an SCR denitration catalyst applicable to glass melter smoke and a preparing method of the SCR denitration catalyst, and belongs to the technical field of SCR denitration catalyst research and development. In the preparing method, titanium dioxide is adopted as a carrier, tungsten triode and vanadium pentoxide which are obtained after predecessor ammonium tungstate and ammonium metavanadate are subjected to pyrolysis are regarded as an auxiliary and an active component respectively, and finally the catalyst is obtained through modification under doping of one or more of oxides of Ce, Mn and Mo. According to the SCR denitration catalyst applicable to glass melter smoke and the preparing method of the SCR denitration catalyst, the doping-modification property which transition metal elements have is utilized, and a reaction temperature window of a catalyst system is adjusted so that the catalyst can maintain a high catalytic activity at the temperature of 300 DEG C-400 DEG C; meanwhile, the resistance of the catalyst to alkali metal poisoning is improved, and thus the catalyst can better promote a denitration reaction in an environment of the glass melter smoke. As experimental data shows, the denitration rate of the prepared catalyst in a simulated environment of the glass melter smoke reaches 80% or above.

Description

technical field [0001] The invention belongs to the technical field of research and development of SCR denitration catalysts, in particular to an SCR denitration catalyst suitable for flue gas of a glass melting furnace and a preparation method thereof. Background technique [0002] Whether air pollutants can be discharged up to standard has become an important factor restricting the development of enterprises. Under the current technical conditions, SCR denitrification technology has been widely used due to its stable operation, high denitrification efficiency, and low ammonia slip. The core of SCR technology. [0003] The vanadium-based catalysts of the existing public technology use titanium dioxide as a carrier, vanadium pentoxide as a catalyst active component, and tungsten trioxide as a catalyst aid, and then add various additives, such as adhesives, extrusion aids and lubricants etc. to prepare catalysts with certain shape, mechanical strength, specific surface area...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/34B01D53/86B01D53/56
CPCB01J23/002B01D53/8628B01D2258/0283B01J23/34B01J2523/00B01J2523/3712B01J2523/47B01J2523/55B01J2523/68B01J2523/69B01J2523/72
Inventor 袁坚程金树许博
Owner GLASS TECH RES INST OF SHAHE CITY OF HEBEI PROVINCE
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