Pressurized-gasification solid-state wet-type deslagging device for carbonaceous organic material and method
A technology of pressurized gasification and organic matter, which is applied in fixed bed gasification, granular/powdered fuel gasification, and production of combustible gas, etc. Valve wear and other problems, to achieve the effect of appropriate slag discharge temperature, eliminate wear and increase operating rate
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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
[0029] 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
[0031] 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 downward ...
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