Coal fines high-temperature pre-warming method

A pulverized coal, high temperature technology, applied in combustion methods, lighting and heating equipment, fluidized bed combustion equipment, etc., can solve the problems of reducing high temperature air temperature, difficult to achieve, limited mixing, etc., to reduce NOx emissions and achieve stable combustion. The effect of good sex and wide adaptability

Active Publication Date: 2008-04-09
INST OF ENGINEERING THERMOPHYSICS - CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] However, compared with the high-temperature air combustion of gas fuels, there is a problem in the high-temperature air combustion of pulverized coal: the specific heat of pulverized coal is much greater than that of general gas fuels. After mixing pulverized coal with high-temperature air at room temperature, the temperature of high-temperature air will be significantly reduced. To a certain extent, it affects the effect of high temperature air combustion
[0005] Chinese patent application 93107510.6 discloses a fluidized bed pulverized coal pre-combustion heating burner. A small fluidized bed pulverized coal pre-combustion heating chamber is arranged outside the pulverized coal primary air nozzle, in order to burn difficult-to-combustible coal and solve the problem of coal burning. Combustion support is usually required for pulverized boilers at low load
However, since the fuel added to the fluidized bed pulverized coal pre-combustion heating chamber is pulverized coal, its particle size is generally less than 200 μm, instead of the coal with a particle size usually between 0 and 5 mm added in a conventional fluidized bed combustion chamber. Particles, so the characteristics of the conventional fluidized bed combustion chamber are difficult to achieve in the pulverized coal pre-combustion heating chamber
Specifically, the fluidized bed described in the patent application is operated with hot bed material, which is difficult

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0020] Example 1

[0021] Add lean coal pulverized coal and air with a stoichiometric ratio of air / fuel (that is, the ratio of the actual amount of air added to the theoretical combustion air amount of the added fuel) from the middle and lower part of the adiabatic circulating fluidized bed combustion chamber to 0.05, so that part of the coal The pulverized coal is heated to 800°C due to the exothermic combustion of the pulverized coal. The high-temperature pulverized coal enters the cyclone separator with the flue gas, and a small amount of pulverized coal is captured by the cyclone separator and then returned to the circulating fluidized bed combustion chamber through the return feeder. The pulverized coal burner of the pulverized boiler burns.

Example Embodiment

[0022] Example 2

[0023] Anthracite pulverized coal and a small amount of coal particles with a particle size between 0.5 and 10 mm are added from the middle and lower part of the adiabatic circulating fluidized bed combustion chamber, and the mass ratio of coal particles to coal powder is 1:10. Air with a stoichiometric ratio of air / fuel of 0.3 was introduced, and part of the pulverized coal and coal particles were burned to release heat, and the pulverized coal was heated to 1300°C. The pulverized coal and some coal particles enter the cyclone separator with the flue gas, and the coal particles and a small amount of pulverized coal are collected and sent back to the circulating fluidized bed combustion chamber through the return feeder, and the rest of the high temperature pulverized coal and flue gas flow out from the gas outlet of the separator , enter the pulverized coal burner of the pulverized coal boiler for combustion.

Example Embodiment

[0024] Example 3

[0025] Bituminous coal powder and a small amount of river sand with a particle size between 0.2 and 2 mm are added from the middle and lower part of the adiabatic circulating fluidized bed combustion chamber. The mass ratio of river sand and coal powder is 1:20. From the bottom of the circulating fluidized bed combustion chamber Air with a stoichiometric ratio of air / fuel of 0.2 was introduced, and part of the pulverized coal was burned to release heat, and the pulverized coal was heated to 1100 °C. The pulverized coal and part of the river sand enter the cyclone separator with the flue gas. The river sand and a small amount of pulverized coal are collected and sent back to the circulating fluidized bed combustion chamber through the return feeder. The rest of the high-temperature pulverized coal and flue gas flow out from the gas outlet of the separator. , enter the pulverized coal burner of the pulverized coal boiler for combustion.

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Abstract

The invention relates to a coal powder high temperature preheating method which relates to the technology of coal powder combustion. The coal powder is added in the middle and lower part of the firebox of an insulating circulating fluid bed and little air is conducted in the bottom part; a part of the coal powder is burnt. The coal powder is heated to between 800 DEG C and 1300 DEG C and the high temperature coal powder enters a cyclone separating device with the flue gas; a part of the coal powder is collected by the cyclone separating device and returned to the firebox through a material returning device; the rest coal powder is sprayed into an inflamer of a coal powder boiler with the flue gas to burn. The invention has the advantages of broad application, good combustion stability and can also cooperate with a classified air distribution technology to control the uniformities of the temperature level and distribution of a furnace, thereby greatly reducing the exhausting of NOx.

Description

technical field [0001] The invention relates to the technical field of combustion, and relates to a pulverized coal combustion method, in particular to a pulverized coal high-temperature preheating method. technical background [0002] In the early 1990s, Japan’s Tanaka et al. proposed high-temperature air combustion technology. The air used for combustion can recover the waste heat of the flue gas to the maximum extent, so that the air temperature can be preheated to above 800°C; at the same time, the fuel is burned in a low-oxygen atmosphere. Realize ultra-low emission of NOx. This combustion method has the dual advantages of high efficiency, energy saving and low pollution emission. Practice shows that the energy saving of gas fuel can reach 60%, and the pollutant emission can be reduced by 25%. High-temperature air combustion technology has achieved good environmental and economic benefits in the industrial application of gas fuels. [0003] In 1999 and 2002, the Japan...

Claims

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Application Information

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IPC IPC(8): F23C10/04
Inventor 吕清刚朱建国牛天钰高鸣宋国良那永洁孙运凯
Owner INST OF ENGINEERING THERMOPHYSICS - CHINESE ACAD OF SCI
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