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Method for desulphurizing, denitrating and decoking fire coal

A desulfurization, denitrification, and coal-fired technology, which is applied in the coke cleaning integrated effect, has the field of desulfurization and denitrification, and can solve the problems of insignificant effect, poor desulfurization effect, and low desulfurization rate.

Inactive Publication Date: 2013-01-23
广州中科高成环保科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] 3. The single sulfur fixation and desulfurization technology in combustion fails to solve the problem of sulfur fixation and secondary release in the high temperature area above 900 °C, the desulfurization rate is low, and the desulfurization effect is not good
Although the synergist can also realize the functions of coal saving, desulfurization and coke cleaning at the same time, its effect is not significant

Method used

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  • Method for desulphurizing, denitrating and decoking fire coal
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  • Method for desulphurizing, denitrating and decoking fire coal

Examples

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Embodiment 1

[0088] A method for preparing a synergist, first adding calcium carbonate, magnesium oxide, silicon oxide, zinc oxide, manganese dioxide, aluminum oxide, and barium hydroxide in sequence and stirring for 10 minutes, and then adding calcium oxide and potassium permanganate And stir for 8 minutes to mix well. The synergist component contains mass percentage: 8% calcium carbonate, 12% magnesium oxide, 10% silicon dioxide, 10% zinc oxide, 10% manganese dioxide, 32% calcium oxide, 7% barium hydroxide, aluminum oxide 3%, potassium permanganate 8%.

[0089] When changing the current smoke exhaust process and equipment, we only start with the combustion of raw coal. According to the physical and chemical indicators of the user's coal, 2‰ (weight ratio) synergist is mixed into the raw coal and put into the boiler for combustion. Some components of the synergist decompose at high temperature, gasify and produce micro-explosion, agitate the pulverized coal and the gas in the pulverized ...

Embodiment 2

[0094] A method for preparing a synergist, first adding calcium carbonate, magnesium oxide, silicon oxide, zinc oxide, manganese dioxide, aluminum oxide, and barium hydroxide in sequence and stirring for 11 minutes, and then adding calcium oxide and potassium permanganate And stir for 8 minutes to mix well. The synergist component contains mass percentage: 25% calcium carbonate, 15% magnesium oxide, 5% silicon dioxide, 5% zinc oxide, 8% manganese dioxide, 15% calcium oxide, 10% barium hydroxide, aluminum oxide 8%, potassium permanganate 9%.

[0095]A kind of preparation method of catalytic activator, first active calcium oxide, iron oxide, zinc oxide are mixed and stirred for 8 minutes and packed into packaging bag, then activated carbon, calcium ammonium nitrate are packed into each packaging bag in proportion, the present embodiment In the process, plastic woven bags are used to pack the catalytic activator, each bag is 25 kg. Before the catalytic activator is put into the ...

Embodiment 3

[0097] A method for preparing a synergist, first adding calcium carbonate, magnesium oxide, silicon oxide, zinc oxide, manganese dioxide, aluminum oxide, and barium hydroxide in sequence and stirring for 11 minutes, and then adding calcium oxide and potassium permanganate And stir for 9 minutes to mix well. The synergist component contains mass percentage: calcium carbonate 10%, magnesium oxide 5%, silicon dioxide 8%, zinc oxide 8%, manganese dioxide 9%, calcium oxide 40%, barium hydroxide 5%, aluminum oxide 5%, potassium permanganate 10%.

[0098] A kind of preparation method of catalytic activator, first active calcium oxide, iron oxide, zinc oxide are mixed and stirred for 9 minutes and then packed into packaging bags, then activated carbon and calcium ammonium nitrate are packed into each packaging bag in proportion, the present embodiment In the process, plastic woven bags are used to pack the catalytic activator, each bag is 25 kg. Before the catalytic activator is put ...

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Abstract

The invention discloses a method for desulphurizing, denitrating and decoking fire coal. In the method, in a raw coal burning stage, a synergist is added in an amount of 0.2 to 0.3 weight percent based on the total weight of the raw coal into the fire coal, and a catalytic active agent is added in an amount of 0.002 to 0.008 weight percent based on the total weight of the raw coal into a slurry boax in a desulphurizing system at the same time. The synergist comprises 8 to 25 mass percent of calcium carbona, 5 to 15 mass percent of magnesium oxide, 5 to 10 mass percent of silicon dioxide, 5 to10 mass percent of zinc oxide, 8 to 10 mass percent of manganese dioxide, 15 to 40 mass percent of calcium oxide, 5 to 10 mass percent of barium hydroxide, 3 to 8 mass percent of aluminum oxide and 8to 15 mass percent of potassium permanganate; and the catalytic active agent comprises 0 to 40 mass percent of active calcium oxide, 20 to 30 mass percent of active carbon, 10 to 15 mass percent of calcium ammonium nitrate, 5 to 20 mass percent of ferric oxide and 2 to 10 percent of zinc oxide. Under the condition of not changing the conventional boiler equipment and process, the method can realize fire coal combustion-supporting and coal-saving functions at one time so as to perform desulphurization, denitration and decoking.

Description

technical field [0001] The invention relates to the field of desulfurization and denitrification, in particular to a method with integrated functions of desulfurization, denitrification and coke cleaning in the coal burning process. Background technique [0002] At present, there is no combustion-supporting coal-saving, SO 2 , NO x , emission reduction, dust removal and coke removal and other methods, the single-function desulfurization technology has the following types: [0003] 1. Desulfurization before combustion: desulfurize the raw coal by concentrated water washing, molding and other methods. The main problem is that the structural sulfur or organic sulfur in coal cannot be removed: and the cost is high, especially the coal used in power plants cannot be used. [0004] 2. Flue gas desulfurization: mainly using flue gas desulfurization devices. Existing problems are huge cost, high operating cost, and secondary pollution. [0005] Wet limestone gypsum process and ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10L9/10
Inventor 陈佐会雷宏洲雷积寿张志洪陈科全
Owner 广州中科高成环保科技有限公司