A Fluidized Bed Lignite Gasification Process with Ash Circulation
A technology of coal gasification and fluidized bed, applied in the field of coal gasification, can solve the problems of unfavorable ash cycle, low efficiency of synthesis gas, complicated process, etc., and achieve the effects of environmental friendliness, less emission of pollutants, and improvement of carbon utilization rate
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Embodiment 1
[0040] A pilot-scale lignite gasification pilot process for 2.5 kg dry basis per hour, using e.g. figure 2 Air conveyed ash circulation shown.
[0041] The temperature of the gasifier is about 1000°C, and the pressure is 0.3MPa. The dried lignite powder (the composition of the coal is shown in Table 1, and the particle size is less than 6mm) is sent into the gasifier through the feed bin, the pressurized feed bin and the screw feeder, and is sent into the gasifier through the N1 port of the dry lignite raw material inlet. The cooled circulating synthesis gas enters the bottom of the gasifier through the circulating synthesis gas inlet N7, and the gas volume is adjusted so that the superficial gas velocity is about 0.1m / s. The function of the circulating syngas is to act as a loosening wind, pushing the pulverized coal upwards. Oxygen after heating (about 1Nm 3 / h) and water vapor (about 1kg / h) enter the gasification furnace through the gasification agent nozzle N2 of diffe...
Embodiment 2
[0051] The lignite gasification test technique and equipment of the same scale as in Example 1, its main difference adopts such as image 3 Mechanically conveyed ash circulation shown. The circulating ash also flows to the vertical screw feeder ⑥ through the feeding pipe ① at the bottom of the gasifier. After the circulating ash is raised to a certain height, it returns to the gasifier through the inclined pipe ⑦ of the circulating ash returning to the gasifier. In addition, since the screw feeder is not resistant to high temperature, it is necessary to install a cooling jacket (not shown in the figure) outside the feeding inclined tube ①. The mass flow rate of the circulating ash can be controlled by the speed of the vertical screw feeder ⑥.
[0052] The ash circulation fluidized bed lignite gasification process described in the above-mentioned embodiment 1 and embodiment 2 is adopted, and the ash content can be returned to the gasifier to continue burning by using air flow...
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