Method for coal slime combustion of circulating fluidized bed boiler

A circulating fluidized bed and boiler combustion technology, which is applied to fluidized bed combustion equipment, combustion methods, fuels burned in a molten state, etc., can solve problems such as improper control of material layer thickness, damage to the heating surface at the tail, and distance from the heating surface of the screen, etc. problems, to achieve the effect of easy burning through, heating and uniform combustion

Inactive Publication Date: 2014-04-02
BEIJING XINGQIAO INT ENG TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] 1. The cross-sectional diameter of the slime flow vertically downward from the furnace top ranges from 150mm to 300mm. What flows out from the slime pipe is a cylindrical slime fluid, which slowly spreads in the air. The central granules are often only dried with water and the surface is burned to form ash shells without burning through. The unburned granules are deposited on the bed material layer at the bottom of the boiler furnace. The granules burn in the bed material at high temperature and agglomerate and are easy to block when they grow up. The slag outlet causes poor slag discharge
[0007] 2. The coal slime flow vertically down from the furnace top must pass through the furnace outlet and be close to the furnace outlet. The furnace outlet is a negative pressure flue gas, which has an attractive effect on the slime flow. The fine carbon particles in the coal slime have not had time to burn. It is drawn away by the negative pressure airflow at the outlet of the furnace and flows to the tail flue of the boiler, causing fine carbon particles to accumulate in the tail flue
[0008] 3. When the fine carbon particles accumulate heavily at the tail, they will burn and cause damage to the heating surface of the tail, resulting in large direct and indirect losses
[0009] 4. The slime flow vertically down from the furnace top must pass through the panel heating surface, and the vertical slime flow is close to the panel heating surface. The slime particles tend to stick to the panel heating surface and accumulate more and more. Affect heat transfer; the slime flow vertically down from the furnace roof passes between the

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  • Method for coal slime combustion of circulating fluidized bed boiler
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  • Method for coal slime combustion of circulating fluidized bed boiler

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Embodiment Construction

[0035] like figure 1 , figure 2 , image 3 Shown, a kind of circulating fluidized bed boiler combustion slime method of the present invention, it comprises the following steps:

[0036] 1. The coal slime from the high-pressure coal slime conveying pipeline 1 enters the furnace 3 through the honeycomb slime inlet 2, so that the slime flow changes from one stream to multiple streams, and it is easy to disperse into rod-shaped slime balls during the falling process, which is heated and combustion evenly, easy to burn through; avoiding the deposition of large coal slime granules that have not burned through in the bed material layer 4 and blocking the slag discharge port 8 resulting in poor slag discharge.

[0037] 2. The honeycomb slime inlet 2 is arranged below the furnace outlet 5, so that the honeycomb slime inlet 2 is far away from the furnace outlet 5, and the honeycomb slime inlet 2 is also far away from the screen heating surface 6. The location of the honeycomb slime i...

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Abstract

The invention discloses a method for coal slime combustion of a circulating fluidized bed boiler. A cellular coal slime pipe orifice is designed to split a stream of coal slime into a plurality of streams, and is positioned below an outlet of a hearth and in the upper part of the hearth in a height direction, the coal slime is horizontally thrown by a reciprocating mechanism leaning against a coal slime pipe section after entering the hearth of the boiler, a layer of upper primary air is arranged on the upper part of the hearth, the thickness of a material layer is properly regulated and controlled to be 450mm to 550mm during the running of the boiler, the volumes of primary air and secondary air are properly regulated and controlled to ensure that the oxygen content of flue gas is 2 to 3 percent, and the negative pressure of the flue gas at the outlet of the hearth is regulated and controlled to be 0 to 50Pa. The method has the advantages that the coal slime flow is prevented from getting close to the outlet of the hearth and a screen type heated surface, the point of fall of the coal slime flow is prevented from being close to a deslagging hole, the concepts of low air volume, low oxygen content, low hearth outlet negative pressure, proper material layer thickness and the like are used for guiding running and regulation, and the operation method is innovative.

Description

technical field [0001] The invention clearly relates to a circulating fluidized bed boiler, in particular to a method for burning coal slime in a circulating fluidized bed boiler. Background technique [0002] my country is currently the country that uses the most circulating fluidized bed boilers (referred to as CFB boilers) in power plants in the world, with a total installed capacity of 100 million kilowatts. There are more than 140 large-scale circulating fluidized bed power plant boilers above h, and more than 100 large-scale circulating fluidized bed power plant boilers above 1025t / h (more than 100 are under construction). [0003] Coal slime is a waste product of coal washing plants in coal mines. Its water content is as high as 30%, its particle size is small, its calorific value is very low, and its ash content is large. Slime method. [0004] The lower part of the furnace of the circulating fluidized bed boiler in the power station is a cone, and the middle and up...

Claims

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Application Information

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IPC IPC(8): F23C10/22F23C10/18
Inventor 张全胜安洋李勇
Owner BEIJING XINGQIAO INT ENG TECH
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