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Desulfurization system of circulating fluidized bed boiler

A kind of technology of circulating fluidized bed and desulfurization system

Active Publication Date: 2013-09-04
CHNA ENERGY INVESTMENT CORP LTD +2
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] However, in the above injection positions, the pressure in the furnace is basically in the positive pressure range, which makes it difficult to inject the desulfurizer. The desulfurizer needs to be transported by high-pressure wind and pneumatically before it can enter the boiler.
Due to the large suspension concentration of pneumatic conveying, the fluidization performance of the desulfurizer is poor, and the state of pneumatic conveying is unstable, resulting in poor desulfurization effect; High power consumption, severe pipeline wear, and desulfurizers such as limestone are easy to absorb moisture and harden, often causing pipeline blockage
At the same time, due to the endothermic calcination and decomposition after the desulfurizer is put in, the bed temperature of the circulating fluidized bed boiler decreases, which leads to the deterioration of the combustion state in the dense phase zone to a certain extent

Method used

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  • Desulfurization system of circulating fluidized bed boiler

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Embodiment Construction

[0034] Specific embodiments of the present invention will be described in detail below in conjunction with the accompanying drawings. It should be understood that the specific embodiments described here are only used to illustrate and explain the present invention, and are not intended to limit the present invention.

[0035] In the present invention, unless stated otherwise, the used orientation words such as "up, down" usually refer to figure 1 Higher and lower positions shown in height direction.

[0036] Such as figure 1 As shown, the specific embodiment of the present invention provides a desulfurization system of a circulating fluidized bed boiler, the desulfurization system includes a cyclone separator 12, the upper part of the cyclone separator 12 is connected with the upper part of the furnace 11 of the boiler, and the The lower part of the cyclone separator 12 is connected to the lower part of the furnace 11 through the return pipe 13, wherein the return pipe 13 ha...

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Abstract

The invention discloses a desulfurization system of a circulating fluidized bed boiler. The desulfurization system comprises a cyclone separator (12), wherein the upper part of the cyclone separator (12) is connected with the upper part of a hearth (11) of the boiler; the lower part of the cyclone separator (12) is connected with the lower part of the hearth (11) through a material returning pipe (13); the material returning pipe (13) is provided with a desulfurization agent inlet (10); and the desulfurization agent inlet (10) is formed in a negative-pressure position of the material returning pipe (13). The desulfurization agent in the desulfurization system can be easily sprayed into the boiler, the desulfurization efficiency is high and the energy consumption is low.

Description

technical field [0001] The invention relates to the field of power generation, in particular to a desulfurization system of a circulating fluidized bed boiler. Background technique [0002] SO 2 As the most important pollutant in the flue gas emitted by the circulating fluidized bed boiler of the coal-fired power plant, its emission is subject to strict restrictions. Therefore, the circulating fluidized bed boiler of the coal-fired power plant is usually equipped with a desulfurization system to reduce The exhaust gas produced by coal is desulfurized, so as to ensure the efficient and reliable operation of the flue gas desulfurization system and reduce environmental pollution. [0003] Circulating fluidized bed boiler is a device that uses clean and efficient low-quality coal to generate electricity. It usually uses flue gas desulfurization by adding limestone and other desulfurizers to the boiler for desulfurization, and the desulfurization efficiency can reach 90%. The b...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/83B01D53/50
Inventor 姚一平王蜀湘白继亮杨海瑞陶世健谢泽良邹利强邱建能杨杰
Owner CHNA ENERGY INVESTMENT CORP LTD
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