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Combustion method and combustion device for desulfuration and denitration of circulating fluid bed

A technology of circulating fluidized bed and combustion method, which is applied in the direction of fluidized bed combustion equipment, combustion method, fuel burned in a molten state, etc., can solve the problem that emissions cannot be satisfied at the same time, and achieve small footprint, simple system, and engineering The effect of low investment cost

Inactive Publication Date: 2017-05-10
INST OF ENGINEERING THERMOPHYSICS - CHINESE ACAD OF SCI
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  • Abstract
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  • Claims
  • Application Information

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Problems solved by technology

Although this method can effectively reduce the emission of nitrogen oxides, it still cannot meet the needs of removing sulfur compounds in flue gas at the same time.

Method used

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  • Combustion method and combustion device for desulfuration and denitration of circulating fluid bed
  • Combustion method and combustion device for desulfuration and denitration of circulating fluid bed
  • Combustion method and combustion device for desulfuration and denitration of circulating fluid bed

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Embodiment Construction

[0029] In this field, the excess air ratio refers to the ratio of the amount of air actually used during combustion to the amount of air that should be theoretically used when the fuel is fully combusted. Since the mixing of fuel and air in the combustion process cannot achieve the ideal degree of uniformity, when the excess air coefficient is equal to 1, the fuel cannot be completely burned. In the engineering practice of boiler design and operation, the excess air coefficient at the furnace outlet is generally selected as 1.2 or so, so the air consumption when the excess air coefficient is equal to 1 is called the theoretical combustion air volume, and the air consumption when the excess air coefficient is equal to 1.2 is called the conventional combustion air volume. In the present invention, both the air for combustion and the air for post-combustion refer to air.

[0030] Among the present invention, the fluidization velocity refers to the commonly used air fluidization v...

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Abstract

The invention discloses a combustion method and a combustion device for desulfuration and denitration of a circulating fluid bed. The combustion method comprises the following steps: a fuel, a desulfurizing agent, and combustion air with the quantity being higher than theoretical combustion air quantity and lower than routine combustion air quantity are supplied to a lower area of a hearth of the circulating fluid bed; a gas and solid mixture generated by combustion in the hearth of the circulating fluid bed enters a cyclone separator from the upper part of the hearth, particles in the gas and solid mixture are separated and sent back to the hearth of the circulating fluid bed, smoke in the gas and solid mixture flows into a tail flue via a center barrel at the top of the cyclone separator and then via an exit flue; complementary combustion air nozzles are formed in the part of the hearth, at the height where a fluidizing velocity is 2.5-4 times that of an air distribution plate, of the circulating fluid bed, and formed in the upper part of the hearth, and / or in an inlet section of the cyclone separator, and complementary combustion air is supplied to the complementary combustion air nozzles. The combustion device has the characteristics of system simplicity, low project investment cost, small floor area, and the like.

Description

technical field [0001] The invention relates to a combustion method and device for a circulating fluidized bed boiler, in particular to a combustion method and device for combined desulfurization and denitrification in a circulating fluidized bed boiler. Background technique [0002] Sulfur dioxide and nitrogen oxides (NOx) are important air pollutants and important substances that cause acid rain and photochemical pollution. When sulfur dioxide enters the atmosphere and reaches a certain concentration, it will cause harm to humans, animals and plants; more importantly, when the relative humidity is high and there are particulate matter, it will undergo a catalytic oxidation reaction to generate SO 3 And sulfuric acid mist, which is 10 times more toxic than sulfur dioxide. The total amount of nitrogen oxide emissions from coal-fired boilers is less than that of sulfur dioxide, but its potential harm to the environment is more serious than that of sulfur dioxide. Among them,...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F23C10/10F23C10/18F23L9/00F23J15/00F23J15/02
CPCF23C10/10F23C10/18F23C2206/10F23C2900/06041F23J15/003F23J15/02F23J2215/10F23J2215/20F23L9/00
Inventor 李诗媛涂秋亚周托王海刚那永洁包绍麟
Owner INST OF ENGINEERING THERMOPHYSICS - CHINESE ACAD OF SCI