CN1660977A - High performance desulfurization and eliminating pollution of fly ash inside coal burning boiler in electric power plant - Google Patents
High performance desulfurization and eliminating pollution of fly ash inside coal burning boiler in electric power plant Download PDFInfo
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- CN1660977A CN1660977A CN 200410049920 CN200410049920A CN1660977A CN 1660977 A CN1660977 A CN 1660977A CN 200410049920 CN200410049920 CN 200410049920 CN 200410049920 A CN200410049920 A CN 200410049920A CN 1660977 A CN1660977 A CN 1660977A
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- coal
- furnace
- slag
- power plant
- multifunctional additive
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Abstract
A process for effective desulfurizing in the boiler using coal as fuel in electric power plant and eliminating the pollution of powdered coal ash features that a multifunctional additive is jetted directly in the boiler or fed into the boiler in conjunction with coal for combining it with SiO2, Al2O3, Fe2O3 and GaO to become new minerals, so effective desulfurizing while modifying the powdered coal ash to become hydraulic cementing material.
Description
Firstly, the power plant boiler is used for efficiently desulfurizing and eliminating the pollution of fly ash, and relates to the technical field of environmental protection, electric power and building material subjects.
Secondly, the technical background is as follows:
since the innovation of China is open, the development of industry, agriculture, traffic and energy sources is rapid and vigorous. The development of industrial and agricultural electric power needs to be advanced, the development of electric power industry in China mainly depends on coal energy, the coal-fired boiler is used for generating electricity accounting for 80 percent of the total generated energy, the nuclear power generation is just started in China, the resource problem of water in water conservancy power generation is solved, the development of coal-fired thermal power generation, the flue gas pollution of the coal-fired boiler and the SO contained in main source coal cannot be kept up with2According to the statistics of the national statistical office, the SO discharged by China currently2More than 3000 million tons, more than the first in the United states, the loss caused by acid rain reaches 1300 million yuan per year, which is equivalent to ton of SO2Loss of 5000 Yuan, foreign to SO2The loss evaluation is $ 3000, which is a great problem affecting the coal-fired development, and national policy determines the atmospheric SO discharged by the coal-fired of industrial enterprises2The concentration must be controlled in the state regulation SO2The emission concentration is below the standard and does not reach the standard for a long time, and the country does not allow the energy-consuming households to survive.
The power industry is fast in thermal power development, and mainly uses coal for power generation and heating. The second difficulty of thermal power generation is that a great deal of methods are needed to solve the problem that a great deal of fly ash is removed after the coal is combusted in the boiler, most of the fly ash is not utilized, the ash is accumulated to occupy a great deal of farmland, and the environment is also influenced to cause great pollution.
Therefore, the coal-fired boiler of the power plant discharges a large amount of SO2And the utilization of fly ash, which are two problems until the problem is solved.
Third, the main contents of the invention
The high-efficiency desulfurization and the elimination of the pollution of the pulverized coal ash in the boiler of the power plant mainly solve two major problems of the desulfurization of the coal-fired power plant and the pollution of the pulverized coal ash, namely two main contents of technical problems.
The multifunctional additive is directly injected into the furnace from the wall of the high-temperature furnace or is mixed with coal, and is injected into the furnace or fed into the furnace, the fuel is mixed and combusted, after the high-temperature combustion, the coal particles and the multifunctional additive fine particles move violently in the furnace, the contact points and the contact surfaces collide violently, reactants and the reacted reactants diffuse and migrate through a product layer, the reaction speed is accelerated, and the coal ash oxide SiO is enabled to be2、Al2O3、Fe2O3CaO and multifunctional additive are oxidized to synthesize new mineral compositions, thereby achieving the purposes of high-efficiency desulfurization in the furnace and modification of ash slag into hydraulic cementing material, high value-added product, and elimination of SO of second pollution of power plant2And fly ash contamination.
(1) The coal material is mixed and burnt at high temperature in the powder furnace, and a great amount of SO is released during the burning of the coal in the furnace2The additive has various functions of catalysis, combustion supporting and desulfurization, and also has active metal oxide, so that the original insufficient combustion condition is changed, the coal can be fully combusted in the furnace, not only a large amount of heat energy is released, but also the carbon content of the fly ash residue is greatly reduced, and moreimportantly, the carbon content is combined under the action of a strong oxidant
(2) The coal material is mixed and burnt at high temperature in the furnace to lead the fly ash oxide SiO to be burnt2、Al2O3、Fe2O3CaO and a multifunctional additive strong oxide are combined into a plurality of new minerals, the modified ash becomes a hydraulic cementing material and becomes a high value-added product, and the modified fly ash can be fully utilized by 100 percent. As the ash residue field is not used, a large amount of farmlands can be saved, the surrounding environment is improved, and the strategic policy of national sustainable development is met.
(3) Before and after the modified ash is produced, an excitant is added, the excitant breaks Si-O bonds and Ai-O bonds, so that the activity of the modified ash can be obviously improved, and the excitant is added to promote fly ash-Ca (OH)2The reaction rate is improved, and the excitant is used for modifying fly ash residue-Ca (OH)2The effect of (3) promotes the disintegration of the vitreous body ofthe modified fly ash. The reaction speed of various substances is improved, and the substances react with the substances of the system to form a new mineral composition. Accelerating the firm formation of the modified fly ash residue gel material.
(4) The technology realizes a short evaluation project with low investment, short construction period and quick response, improves the environmental protection benefit and the economic benefit of enterprises and society, and has wide development prospect.
Claims (5)
1. A technology for high-efficiency desulfurizing and eliminating the pollution of powdered coal ash in coal-fired boiler of electric power plant features that the multifunctional additive and coal are burnt at high temp in furnace to combine the oxide of coal ash and the oxide of multifunctional additive into a new mineral composition, resulting in high-efficiency desulfurizing and modifying powdered coal ash to become high-value-added hydraulic cementing material.
2. The method of claim 1: the multifunctional additive is directly injected into the furnace from four positions of the high-temperature furnace wall or is mixed with coal and injected into the furnace or fed into the furnace.
3. The method of claim 2: the multifunctional additive is characterized by comprising minerals, limestone, quicklime, wollastonite, pumice, waste slag discharged by smelting rare metals, iron-manganese-silicon slag, zinc slag, silicon slag, magnesium slag, nickel slag, manganese slag, chemical by-product sodium sulfate, calcium chloride and potassium oxide, and has the main functions of: catalysis, desulfurization and combustion supporting.
4. The method of claim 3: ratio range of multifunctional additive to coal
Additive coal
(5~55)∶(95~45)。
5. The method of claim 4: the technology for high-efficiency desulfurization and eliminating pollution of fly ash in coal-fired boiler of power plant is applicable to three types of circulating fluidized bed boiler, pulverized coal furnace and cyclone furnace.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN 200410049920 CN1660977A (en) | 2004-06-18 | 2004-06-18 | High performance desulfurization and eliminating pollution of fly ash inside coal burning boiler in electric power plant |
Applications Claiming Priority (1)
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CN 200410049920 CN1660977A (en) | 2004-06-18 | 2004-06-18 | High performance desulfurization and eliminating pollution of fly ash inside coal burning boiler in electric power plant |
Publications (1)
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CN1660977A true CN1660977A (en) | 2005-08-31 |
Family
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Family Applications (1)
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CN 200410049920 Pending CN1660977A (en) | 2004-06-18 | 2004-06-18 | High performance desulfurization and eliminating pollution of fly ash inside coal burning boiler in electric power plant |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101275096B (en) * | 2008-05-21 | 2011-11-02 | 宋云星 | Solid desulfuration incendiary agent for coal-burning boiler |
CN101735878B (en) * | 2009-11-12 | 2012-11-21 | 浙江大学 | High-efficiency coal catalyst and preparation method thereof |
GB2516728A (en) * | 2013-05-10 | 2015-02-04 | Internat Innovative Technologies Ltd | Fuel enrichment process |
CN114797872A (en) * | 2022-04-29 | 2022-07-29 | 清华大学 | Medium-low temperature additive and process for jointly removing nitrous oxide and NOx in furnace |
-
2004
- 2004-06-18 CN CN 200410049920 patent/CN1660977A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101275096B (en) * | 2008-05-21 | 2011-11-02 | 宋云星 | Solid desulfuration incendiary agent for coal-burning boiler |
CN101735878B (en) * | 2009-11-12 | 2012-11-21 | 浙江大学 | High-efficiency coal catalyst and preparation method thereof |
GB2516728A (en) * | 2013-05-10 | 2015-02-04 | Internat Innovative Technologies Ltd | Fuel enrichment process |
GB2516728B (en) * | 2013-05-10 | 2016-01-13 | Internat Innovative Technologies Ltd | Fuel enrichment proces |
CN114797872A (en) * | 2022-04-29 | 2022-07-29 | 清华大学 | Medium-low temperature additive and process for jointly removing nitrous oxide and NOx in furnace |
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