Method for preparing coal tar by carrying out catalytic pyrolysis on pulverized coal and device thereof
A technology of catalytic pyrolysis and coal tar, which is applied in the field of coal chemical industry, can solve problems such as the limitation of scale-up production, achieve the effect of reducing secondary cracking and increasing yield
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Embodiment 1
[0033] in figure 1 In this embodiment, the device for producing coal tar by catalytic pyrolysis of pulverized coal consists of a catalytic pyrolysis reactor 1, a heating riser 2, a circulating gas blower 3, a raw gas purification device 4, a gas blower 5, and a high-temperature semi-coke heat exchanger 6. , The heating furnace 7, the flue gas induced draft fan 8, and the high temperature gas heat exchanger 9 are connected together.
[0034] The upper outlet of the catalytic pyrolysis reactor 1 is connected to the inlet of the raw gas purification device 4 through a pipeline, and the middle outlet is connected to the inlet of the lower end of the heating riser 2 through a valve installed on the pipeline, and is exchanged with high temperature semi-coke through the pipeline. The middle inlet of the heat exchanger 6 is connected, the heating furnace 7 is connected with the inlet of the heating riser 2 through a pipe, the middle outlet of the heating riser 2 is connected with the semi...
Embodiment 2
[0050] In this embodiment, the vertical section of the pyrolysis reaction tube 1-5 of the catalytic pyrolysis reactor 1 and the annular closed partition 1-2 are welded and connected with four cyclone tubes 1-3, the cyclone tubes 1-3 and the heat The dereaction tubes 1-5 are in communication with each other, pass through the flow guide tubes 1-4, and the free ends extend outside the tube wall of the flow guide tubes 1-4, and the free ends are processed into a downward spiral shape. The angle between the oblique wall of the necking section of the outer cylinder 1-6 and the horizontal plane is 36°C. The gas distributor 1-11 of the catalytic pyrolysis reactor 1 is processed with 3 circles of pores arranged in concentric circles. One of the pores in one circle is arranged on the same radius as the one in the adjacent circle. The pores in the circle and the pores in the adjacent circle can also be staggered, and the pore diameter is 12mm. The support plate 1-10 of the catalytic pyro...
Embodiment 3
[0053] In this embodiment, the vertical section of the pyrolysis reaction tube 1-5 of the catalytic pyrolysis reactor 1 and the annular closed partition 1-2 are welded and connected with 8 cyclone tubes 1-3, the cyclone tubes 1-3 and the heat The dereaction tubes 1-5 are in communication with each other, pass through the flow guide tubes 1-4, and the free ends extend outside the tube wall of the flow guide tubes 1-4, and the free ends are processed into a downward spiral shape. The angle between the oblique wall of the necking section of the outer cylinder 1-6 and the horizontal plane is 60°. The gas distributor 1-11 of the catalytic pyrolysis reactor 1 is processed with 20 circles of pores arranged in concentric circles. One of the pores in one circle is arranged on the same radius as the one in the adjacent circle. The pores in the circle and the pores in the adjacent circle can also be arranged staggered, and the pore diameter is 8mm. The support plate 1-10 of the catalytic...
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