Ash agglomeration gasification reaction device

A technology of gasification reaction and air intake device, applied in the field of coal gasification, to achieve full and thorough gas-solid reaction, improve coal gasification efficiency, and facilitate the discharge of ash

Active Publication Date: 2015-03-25
SHANGHAI BOILER WORKS
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, as far as the current exhaust method is concerned, if the gas velocity is too high, it is easy to form channel flow; if the gas velocity is too low, it is easy to leak material or the high temperature area cannot reach the proper high temperature.
Moreover, the center pipe is exposed in the slag discharge channel, which is more likely to stick to dirt and slag and burn, and it is more likely to cause poor slag discharge, etc.

Method used

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  • Ash agglomeration gasification reaction device
  • Ash agglomeration gasification reaction device
  • Ash agglomeration gasification reaction device

Examples

Experimental program
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Embodiment

[0046] Such as figure 1 As shown, it is a schematic structural diagram of an improved ash fusion gasification reaction device provided by the present invention, including an ash fusion gasification system and a slag discharge cooling system. The ash fusion gasification system is composed of gasifier shell 1, coal nozzle 2, fine ash return nozzle 3, ash fusion gas intake device and other main components; the slagging cooling system consists of a slagging chamber 10. The slag discharge tank 12, the water cooling jacket 9 and the lower gasification agent inlet 11 are composed of main components; the ash fusion gasification system is connected to the slag collection chamber 10 through the central slag discharge pipe 8.

[0047] The ash fusion gas inlet device includes two gas inlet chambers inside and outside, two gas inlets, a gas distribution plate 4 and a heat-insulating refractory lining 16 and other structures. Said heat-insulating refractory lining 16, gas distribution pla...

example 1

[0050] Take a coal gasification device with a daily processing capacity of 600 tons of coal as an example, the gasification pressure is 0.6MPa, and the gasification temperature is 1050°C. Coal powder enters from the nozzle 2, water vapor and oxygen enter the air intake chamber from the gasification agent inlet 6 and 7 respectively, and then enter the gasification reaction device through the pores on the corresponding gas distribution plate, and the combustion gasification reaction occurs , of which the oxygen intake is 10200Nm 3 / h, the steam intake is 23200kg / h. The temperature of the gasification reaction device is mainly achieved by adjusting the amount of oxygen in the inner air inlet chamber 14. The gas entering from the inner air inlet chamber 14 accounts for about 75% of the total air intake; the gas entering from the outer air inlet chamber 13 accounts for about 75%. 15% of the total intake air, together with water vapor, mainly controls the fluidization of granular m...

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Abstract

The invention discloses an improved ash agglomeration gasification reaction device comprising an ash agglomeration gasification system comprising a feeding nozzle, a conic gas distributing plate, a gasifying agent air inlet, a double-inlet-chamber air inlet device and the like, and a deslagging and cooling system comprising a slag gathering chamber, a slag discharging tank, a water cooling jacket, a gas inlet and the like. According to the improved ash agglomeration gasification reaction device disclosed by the invention, a center pipe structure which generates slag and is burnt up easily in the ash agglomeration gasification reaction device is saved, the air inlet device of the ash agglomeration gasification reaction device is improved, and the deslagging and cooling system is optimized to facilitate control of deslagging and cooling of ash slag. The gasification reaction device is simple in structure, can run stably for a long time and is higher in gasification efficiency.

Description

[0001] Technical field: [0002] The patent of the invention belongs to the field of coal gasification, and specifically relates to an ash fusion gasification reaction device. [0003] Background technique: [0004] The ash fusion powder coal gasification process uses the principle of fluidization to continuously feed the raw powder coal into the dense phase area of ​​the gasification reaction device, and the gasification agent (pure oxygen, carbon dioxide and steam) is blown in from the bottom of the gasification reaction device to make the coal Particle boiling fluidization. Under the high temperature conditions generated by combustion, the gas-solid two-phase is fully mixed and contacted, and the pyrolysis of coal and the redox reaction of carbon occur, and finally the gasification of coal is realized. The feature of this process is that the high-oxygen oxidizing agent and steam enter the central area of ​​the bed through the center pipe, forming a local high-temperature...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10J3/56
CPCC10J3/56C10J3/72C10J3/76C10J2200/152C10J2300/093
Inventor 李平倪建军乌晓江程相宣
Owner SHANGHAI BOILER WORKS
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