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Low-temperature SCR flue gas denitrification catalyst loaded with manganese oxides on lotus leaf source biochar and preparation method and application thereof

A denitration catalyst, manganese oxide technology, applied in catalyst activation/preparation, metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, etc. Reduce and other problems, achieve good low-temperature SCR activity and stability, improve catalytic activity, and achieve the effects of high social significance

Active Publication Date: 2021-01-19
JIANGXI AGRICULTURAL UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Catalysts are the key to SCR flue gas denitrification technology. At present, commercial SCR catalysts are mainly V 2 o 5 –WO 3 (MoO 3 ) / TiO 2 series of catalysts, the active temperature window is 300-400 ° C, due to the high temperature required, the SCR denitration device is generally placed before the dust removal and desulfurization device, so the catalyst is easily washed and blocked by dust, and the service life is reduced

Method used

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  • Low-temperature SCR flue gas denitrification catalyst loaded with manganese oxides on lotus leaf source biochar and preparation method and application thereof
  • Low-temperature SCR flue gas denitrification catalyst loaded with manganese oxides on lotus leaf source biochar and preparation method and application thereof
  • Low-temperature SCR flue gas denitrification catalyst loaded with manganese oxides on lotus leaf source biochar and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] (1) Pretreatment of lotus leaves:

[0035] Using lotus leaves as raw materials, drying the lotus leaves and pulverizing them with a pulverizer, weighing a certain amount of pulverized lotus leaves, and using nitric acid solution to impregnate the biomass raw materials, the ratio of acid to raw material mass during the impregnation process is controlled to be 1.5 : 1 and then mix with 50mL of deionized water, stir evenly for 2h, and then soak for 14h;

[0036] (2) Preparation of lotus leaf biochar:

[0037] The impregnated and filtered powders were dried at 105 °C for 24 h, and then placed in a tubular resistance furnace under 100 mL / min N 2 Under the protection, the heating rate was 5 °C / min to 800 °C, and the constant temperature was activated for 2 h; after the activation, N continued to be fed. 2 Until the furnace tube reaches room temperature, the primary product of activated carbon is obtained; then, use boiled deionized water to wash until neutral, and dry the w...

Embodiment 2

[0041] (1) Pretreatment of lotus leaves:

[0042] Using lotus leaves as raw materials, drying the lotus leaves and pulverizing them with a pulverizer, weighing a certain amount of pulverized lotus leaves, and using nitric acid solution to impregnate the biomass raw materials, the ratio of acid to raw material mass during the impregnation process is controlled to be 1.5 : 1 and then mix with 50mL of deionized water, stir evenly for 2h, and then soak for 14h;

[0043] (2) Preparation of lotus leaf biochar:

[0044] The impregnated and filtered powders were dried at 105 °C for 24 h, and then placed in a tubular resistance furnace under 100 mL / min N 2 Under the protection, the heating rate was 5 °C / min to 800 °C, and the constant temperature was activated for 2 h; after the activation, N continued to be fed. 2 Until the furnace tube reaches room temperature, the primary product of activated carbon is obtained; then, use boiled deionized water to wash until neutral, and dry the w...

Embodiment 3

[0048] (1) Pretreatment of lotus leaves:

[0049] Using lotus leaves as raw materials, drying the lotus leaves and pulverizing them with a pulverizer, weighing a certain amount of pulverized lotus leaves, and using nitric acid solution to impregnate the biomass raw materials, the ratio of acid to raw material mass during the impregnation process is controlled to be 1.5 : 1 and then mix with 50mL of deionized water, stir evenly for 2h, and then soak for 14h;

[0050] (2) Preparation of lotus leaf biochar:

[0051] The impregnated and filtered powders were dried at 105 °C for 24 h, and then placed in a tubular resistance furnace under 100 mL / min N 2 Under the protection, the heating rate was 5 °C / min to 800 °C, and the constant temperature was activated for 2 h; after the activation, N continued to be fed. 2 Until the furnace tube reaches room temperature, the primary product of activated carbon is obtained; then, use boiled deionized water to wash until neutral, and dry the w...

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Abstract

The invention belongs to the field of environmental protection and environmental catalysis, and in particular relates to a low-temperature SCR flue gas denitrification catalyst loaded with manganese oxide derived from lotus leaf biochar, a preparation method and application thereof. In the present invention, the biochar material is obtained by anaerobically roasting typical agricultural waste lotus leaves after acid modification treatment, using lotus leaf biochar as a carrier, MnO x As the active component, a low-temperature flue gas denitrification catalyst based on lotus leaf biochar was obtained. The biochar prepared by chemical modification has a high specific surface area, and through MnO x The interaction with biochar from lotus leaves improves the denitrification activity of the catalyst; when ammonia is used as the reducing agent and the temperature is 250°C, the SCR activity of the catalyst can approach 90%.

Description

technical field [0001] The invention belongs to the field of environmental protection and environmental catalysis, and in particular relates to a low-temperature SCR flue gas denitrification catalyst with manganese oxide loaded on lotus leaf source biochar and a preparation method and application thereof. Background technique [0002] Nitrogen oxides (NO x ) is one of the major air pollutants. In addition to directly harming human health, it is also one of the important precursors of ozone generation, and it is also an important reason for the formation of regional haze and fine particles. Nitrogen oxides mainly come from the combustion of fossil fuels. According to statistics, 66.7% of the national industrial nitrogen oxide emissions come from the power and heat production and supply industries, which are the largest emitters of nitrogen oxides in my country, of which the thermal power industry contributes Therefore, the power industry is a key area for controlling nitroge...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/34B01J37/02B01J37/08B01J37/34B01D53/86B01D53/56
CPCB01D53/8628B01J23/34B01J37/0207B01J37/084B01J37/343
Inventor 喻成龙
Owner JIANGXI AGRICULTURAL UNIVERSITY