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Modified honeycomb monolithic catalyst for synchronously removing organic waste gas and NOx in coal-fired flue gas as well as preparation method and application of modified honeycomb monolithic catalyst

An integrated catalyst, organic waste gas technology, applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of low mechanical strength of catalyst, large amount of catalyst, cost High problems, to achieve the effect of simple and easy preparation method, wide temperature window and high activity

Active Publication Date: 2021-04-16
SOUTH CHINA UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Commercial SCR catalysts currently mainly include honeycomb, plate and corrugated catalysts, among which honeycomb monolithic extruded catalysts are widely used in the field of industrial flue gas denitrification, but the amount of catalyst is large High cost and low mechanical strength of the catalyst

Method used

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  • Modified honeycomb monolithic catalyst for synchronously removing organic waste gas and NOx in coal-fired flue gas as well as preparation method and application of modified honeycomb monolithic catalyst
  • Modified honeycomb monolithic catalyst for synchronously removing organic waste gas and NOx in coal-fired flue gas as well as preparation method and application of modified honeycomb monolithic catalyst
  • Modified honeycomb monolithic catalyst for synchronously removing organic waste gas and NOx in coal-fired flue gas as well as preparation method and application of modified honeycomb monolithic catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] MoOx-V 2 o 5 -WO 3 / TiO 2 - powder catalyst

[0032] Add 0.0458g of V precursor ammonium metavanadate and 0.1654g of W precursor ammonium tungstate into 30mL of deionized water and mix thoroughly, place in a heat-collecting constant temperature magnetic stirrer and stir for 45min to dissolve, and then Add 1.8 g of oxalic acid precursor under stirring state, and continue to stir vigorously at constant temperature after ultrasonication for 60 min to prepare a mixed precursor solution. Add 0.11 g of ammonium molybdenum molybdate in the stirring state, continue to stir vigorously at constant temperature for 30 minutes after ultrasonication, and prepare a mixed precursor solution; TiO as the catalyst carrier 2 Take out after drying in a vacuum oven, cool to room temperature for use; the TiO 2 The mass is 2g. Add the TiO of the above-mentioned oven-dried carrier under agitation 2 , continue to stir at a constant temperature for 90 minutes until evaporated to dryness, d...

Embodiment 2

[0034] Mo-cordierite monolithic catalyst - impregnated

[0035] Add 0.458g of V precursor ammonium metavanadate and 1.654g of W precursor ammonium tungstate into 60mL of deionized water and mix thoroughly, place in a collector type constant temperature magnetic stirrer at constant temperature and stir for 30min to dissolve, ultrasonic After 60 minutes, continue to stir vigorously at constant temperature to prepare a mixed precursor solution. Add 0.11 g of ammonium molybdate under stirring state, continue to stir vigorously at constant temperature for 30 min after ultrasonication, and prepare a mixed precursor solution; TiO as a catalyst carrier 2 Take out after drying in a vacuum oven, cool to room temperature for use; the TiO 2 The mass is 20g; the cordierite honeycomb ceramics is cut into a sample block with a diameter of 25mm and a height of 8mm. Before loading, all sample blocks were ultrasonically treated, then dried in a vacuum oven, and calcined to remove various adso...

Embodiment 3

[0038] Cu-cordierite monolithic catalyst-silica sol catalyst

[0039] Add 0.458g of V precursor ammonium metavanadate and 1.654g of W precursor ammonium tungstate into 60mL of deionized water and mix thoroughly, place in a heat-collecting constant-temperature magnetic stirrer and stir for 30 minutes to dissolve it. Add 0.8g of oxalic acid precursor under stirring, continue to stir vigorously at constant temperature after ultrasonication for 60min, and prepare a mixed precursor solution; add 5.4g of copper nitrate under stirring, continue vigorously stirring at constant temperature for 30min after ultrasonication, and prepare a mixed precursor solution; TiO will be used as catalyst support 2 Take out after drying in a vacuum oven, cool to room temperature for use; the TiO 2 The mass is 20g; the cordierite honeycomb ceramics is cut into a sample block with a diameter of 25mm and a height of 8mm. Before loading, all sample blocks were ultrasonically treated, then dried in a vac...

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Abstract

The invention discloses a modified honeycomb monolithic catalyst for synchronously removing organic waste gas and NOx in coal-fired flue gas as well as a preparation method and application of the modified honeycomb monolithic catalyst. The method provided by the invention overcomes the defects of large dosage, high cost, low catalyst mechanical strength, narrow temperature window of organic waste gas in high-sulfur, high-nitrogen and high-ammonia flue gas, low activity, low COx selectivity and low oxidation efficiency of the existing commercial extrusion type catalyst, shows excellent oxidation performance on the organic waste gas in the high-sulfur, high-nitrogen and high-ammonia flue gas, and simultaneous removes organic waste gas and NOx. The prepared catalyst can be widely applied to the fields of independent control of organic waste gas and NOx in high-sulfur, high-nitrogen and high-ammonia flue gas, industrial boilers, coal-fired power plants, iron and steel plants and other coal-fired process flue gas, synchronous purification of the organic waste gas and NOx and other atmospheric pollution control.

Description

technical field [0001] The invention belongs to the technical field of environmental functional materials, and specifically relates to a metal composite modified honeycomb monolithic catalyst for synchronously removing organic waste gas and NOx in flue gas of a coal-fired boiler, its preparation method and its application, and its application in high temperature Sulfur, high nitrogen, high ammonia flue gas, separate control of organic waste gas and NOx in flue gas of industrial boilers, coal-fired power plants, steel plants and other coal-fired processes, and synchronous purification of organic waste gas and NOx and other applications in air pollution control. . Background technique [0002] At present, there is a serious lack of understanding of the formation mechanism of organic pollutants in the process of coal combustion at home and abroad, and there is a lack of corresponding control measures. Volatile organic compounds in coal-fired flue gas have complex environmental...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/30B01J23/28B01J23/72B01D53/86B01D53/72
Inventor 胡芸张益兰肖高飞林焙隆付名利
Owner SOUTH CHINA UNIV OF TECH