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Carbonaceous organic material pressurized-gasification solid wet deslagging device and method

A technology for pressurized gasification and organic matter, which is applied in fixed bed gasification, granular/powder fuel gasification, production of combustible gas, etc. Valve wear and other problems, to achieve the effect of suitable slag discharge temperature, elimination of wear and improvement of operating rate

Inactive Publication Date: 2011-05-25
SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] For fixed bed and fluidized bed gasification processes, there are many problems in the existing high-temperature solid-state dry slagging method, which seriously affect the long-term operation of the gasifier: 1) The high-temperature solid material is cooled by gas, which is only suitable for fixed-bed gasification The process is not suitable for fluidized bed; fluidized bed generally adopts water-cooled screw machine, but for large slag discharge, due to indirect heat exchange, a large heat exchange area is required, so multi-stage series connection has to be used, the equipment is complicated, and the mechanical transmission parts It is also easily damaged; 2) For the high-pressure dry slag discharge lock hopper, a large amount of high-pressure gas (nitrogen or CO 2 and other gases), and the dust entrained in the discharge gas during the decompression process causes wear and tear on pipes and valves, and the exhaust gas contains combustible gases and sulfides, which can cause environmental pollution; Severe dust

Method used

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  • Carbonaceous organic material pressurized-gasification solid wet deslagging device and method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] The slag discharge device is composed of an upper slag hopper and a lower slag hopper. There is a high-temperature ash inlet pipe 17 on the top of the upper slag hopper. There is a jacket pipe 1 outside the high-temperature ash inlet pipe 17. There is water or water on the jacket pipe 1. The low-temperature gas inlet 2, the lower end of the annulus of the jacket pipe 1 is an opening, the upper slag hopper temperature measuring port 6, the upper installation port 3 of the liquid level gauge, the lower installation port 5 of the liquid level gauge and the high pressure water overflow port 4 in the middle of the upper slag hopper , the height of the high-pressure water overflow port 4 is located below the upper installation port 3 of the liquid level gauge, there is a high-pressure water inlet 7 and a circulating water inlet 8 at the lower part of the upper slag hopper, and an upper slag hopper slag discharge pipe 18 is located at the bottom of the upper slag hopper. There ...

Embodiment 2

[0030] The high-temperature ash inlet pipe 17 of the slagging device of the present invention is connected to the slag outlet of the gasifier, and the high-temperature ash discharged from the slag outlet of the gasifier enters the high-temperature ash inlet pipe 17, and the slag from the jacket pipe 1 CO2, entraining ash and slag at a speed of 30m / s, falls into the upper slag hopper, and is cooled to 60°C in contact with high-pressure water. The temperature in the upper slag hopper is controlled by the high-pressure water entering the upper slag hopper high-pressure water inlet 7, and the flow rate is 120t / h, the liquid level of the water in the upper slag hopper is controlled by adjusting the high-pressure water discharged from the high-pressure water overflow port 4. In order to ensure that the ash and slag smoothly fall into the lower slag hopper, the water circulation of 15t / h is discharged from the lower slag hopper circulating water outlet 19 Enter the upper slag hopper ...

Embodiment 3

[0032] The high-temperature ash inlet pipe 17 of the slagging device of the present invention is connected to the slag outlet of the gasifier, and the high-temperature ash discharged from the slag outlet of the gasifier enters the high-temperature ash inlet pipe 17, and the slag from the jacket pipe 1 Water vapor (270°C) entrains ash and slag at a speed of 60m / s and falls into the upper slag hopper, contacts with high-pressure water and is cooled to 80°C, and enters the lower slag hopper through the upper valve 10 of the lower slag hopper with the downward water flow; The temperature in the slag hopper is controlled by the high-pressure water entering the high-pressure water inlet 7 of the upper slag hopper, and the flow rate is 200t / h. The slag falls into the lower slag hopper smoothly, and the 30t / h water discharged from the circulating water outlet 19 of the lower slag hopper circulates through the circulating water inlet 8 and enters the upper slag hopper, forming a downwar...

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Abstract

The invention relates to a carbonaceous organic material pressurized-gasification solid wet deslagging device comprising an upper slag bucket and a lower slag bucket, wherein the top end of the upper slag bucket is provided with a high-temperature ash inlet pipe (17); a jacket pipe (1) is arranged outside the high-temperature ash inlet pipe (17) and provided with a water or low-temperature gas inlet (2); the lower end of the annular gap of the jacket pipe (1) is open; the middle of the upper slag bucket is provided with an upper slag bucket temperature measuring port (6), a liquidometer upper mounting port (3), a liquidometer lower mounting port (5) and a high-pressure water overflow port (4); the high-pressure water overflow port (4) is lower than the liquidometer upper mounting port (3); the lower part of the upper slag bucket is provided with a high-pressure water inlet (7) and a circulating water inlet (8); the bottom of the upper slag bucket is provided with an upper slag bucket slag drop pipe (18) which is provided with a loose water inlet (9); a lower slag bucket upper valve (10) is connected with the upper slag bucket slag drop pipe (18) and a lower slag bucket slag drop pipe (13); the lower slag bucket slag drop pipe (13) is positioned in the middle of the top of the lower slag bucket; two sides of the lower slag bucket slag drop pipe (13) at the top of the lower slag bucket are provided with a pressure measuring port (11) and a depressurizing port (12); the upper part of the lower slag bucket is provided with a lower slag bucket pressurizing water inlet (14) and a circulating water outlet (19); the middle of the lower slag bucket is provided with a lower slag bucket temperature measuring port (15); and the bottom of the lower slag bucket is provided with a lower slag bucket lower valve (16). The invention has the advantages of simple structure, low maintenance amount, long operation cycle and friendly operating environment.

Description

technical field [0001] The invention relates to a solid-state wet slag discharge device and method for pressurized gasification of carbon-containing organic matter, in particular to a cooling and discharge device and method for high-temperature and high-pressure ash during the solid-state slag discharge gasification process. Background technique [0002] Coal gasification technology is widely used in chemical industry, metallurgy, machinery, building materials and civil gas, etc., and is the leading technology in these industries. [0003] Coal gasification technology can be divided into three categories according to the movement state of raw coal in the gasifier: moving bed, fluidized bed and entrained bed. In the fixed bed, the block coal and the gasification agent are added in reverse. After the carbon and other organic matter in the coal are gasified, the ash will be discharged from the bottom of the furnace. Discharge in solid state, if the ash and slag flow out in a l...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10J3/54C10J3/56C10J3/46C10J3/52C10J3/34C10J3/06
Inventor 黄戒介王毅房倚天原丰贞王洋宋新朝张永奇刘于英杨金权郭金霞马小云张尚武王志宇
Owner SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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