Method and device for preparing water gas by using wastewater and gasification of partial semi-coke powder
A technology of water gas and semi-coke, applied in the field of coal chemical industry, can solve the problems of increasing operating costs, large investment, and increasing costs, and achieve the effects of reducing operating costs, saving water resources, and avoiding pollution
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Embodiment 1
[0027] exist figure 1 Among them, the device for preparing water gas by gasification of waste water and part of semi-coke powder in the present embodiment consists of heating riser 1, No. I cyclone separator 2, waste heat boiler 3, airflow part gasification pipe 4, No. II cyclone separator 5, waste heat boiler The gas purification device 6 and the steam generator 7 are connected to form.
[0028] The outlet of the heating riser 1 communicates with the lower inlet of the No. I cyclone separator 2 through the pipeline, the upper outlet of the No. I cyclone separator 2 communicates with the lower inlet of the waste heat boiler 3 through the pipeline, and the side wall outlet is installed on the pipeline through the The valve of the valve is connected with an inlet of the side wall of the gasification tube 4 of the gas flow part, the outlet of the side wall of the waste heat boiler 3 is connected with the bottom inlet of the gasification tube 4 of the gas flow part through a pipel...
Embodiment 2
[0041] In this embodiment, the angle α between the side wall of the first stage umbrella distributor 7-5 of the steam generator 7 and the horizontal plane 1 is 30°, the ratio of the inner diameter D2 of the bottom surface of the first-stage umbrella-shaped distributor 7-5 to the inner diameter D1 of the hot coke powder inlet pipe 7-2 is 1, and the side wall of the first-stage bucket-shaped distributor 7-9 and The angle α between the horizontal plane 2 is 30°, the ratio of the inner diameter D3 of the lower end opening of the first-stage bucket distributor 7-9 to the inner diameter D1 of the hot coke powder inlet pipe 7-2 is 2, and the ratio of the second-stage umbrella distributor 7-11 to the first The structure of the stage umbrella distributor 7-5 is identical, and the structure of the second stage bucket distributor 7-14 is identical to that of the first stage bucket distributor 7-9. The lower 3 / 4 side walls of the vertical height of the first-stage bucket distributor 7-9 ...
Embodiment 3
[0044] In this embodiment, the angle α between the side wall of the first stage umbrella distributor 7-5 of the steam generator 7 and the horizontal plane 1 is 60°, the ratio of the inner diameter D2 of the bottom surface of the first-stage umbrella-shaped distributor 7-5 to the inner diameter D1 of the hot coke powder inlet pipe 7-2 is 2, and the side wall of the first-stage bucket-shaped distributor 7-9 and The angle α between the horizontal plane 2 is 60°, the ratio of the inner diameter D3 of the lower end opening of the first-stage bucket-shaped distributor 7-9 to the inner diameter D1 of the hot coke powder inlet pipe 7-2 is 3, and the ratio of the second-stage umbrella-shaped distributor 7-11 to the first The structure of the stage umbrella distributor 7-5 is identical, and the structure of the second stage bucket distributor 7-14 is identical to that of the first stage bucket distributor 7-9. The lower 3 / 4 side walls of the vertical height of the first-stage bucket di...
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