Pulverized-coal and liquification residue co-pyrolysis dust removing system and method
A technology for coal liquefaction residue and liquefaction residue, which is applied to the mechanical treatment of coal loaded into the furnace, the purification of combustible gas, and the prevention/removal of fouling in the furnace. The waste of pulverized coal or semi-coke can improve the utilization rate of raw materials and reduce the energy consumption of pyrolysis.
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Embodiment 1
[0055] Using the system of the present invention, the pulverized coal with a particle size of less than 6mm and the liquefied residue at 290°C from the liquefied residue dust removal unit are sprayed into the fast pyrolysis furnace through the pulverized coal inlet 11 and the liquefied residue inlet 12 respectively, and the pulverized coal is sprayed into the fast pyrolysis furnace. The mass ratio of the reaction with the liquefied residue is 1:0.3, and the mixed material passes through the low-temperature dry distillation section and the high-temperature dry distillation section of the fast pyrolysis furnace sequentially under the action of gravity; wherein, the temperature of the low-temperature dry distillation section is 550-600°C, and the high-temperature dry distillation section The temperature of the section is 870-900°C; in the low-temperature dry distillation section, the liquefied residue is basically pyrolyzed completely, while the coal powder undergoes mild pyrolysis...
Embodiment 2
[0058] This embodiment is the same as the system used in the above-mentioned embodiment 1, but the process conditions are different, as described below. Spray pulverized coal with a particle size of less than 6mm and liquefied residue at 360°C from the liquefied residue dust removal unit into the fast pyrolysis furnace through the pulverized coal inlet 11 and the liquefied residue inlet 12, and react the pulverized coal with the liquefied residue The mass ratio of the mixture is 1:0.5, and the mixed materials rely on gravity to pass through the low-temperature dry distillation section and the high-temperature dry distillation section of the fast pyrolysis furnace in turn; among them, the temperature of the low-temperature dry distillation section is 650-700°C, and the temperature of the high-temperature dry distillation section is 900- 950℃; in the low-temperature dry distillation section, the liquefied residue is basically completely pyrolyzed, while the coal powder undergoes ...
Embodiment 3
[0061] This embodiment is the same as the system used in the above-mentioned embodiment 1, but the process conditions are different, as described below. Spray pulverized coal with a particle size of less than 6mm and liquefied residue at 240°C from the liquefied residue dust removal unit into the fast pyrolysis furnace through the pulverized coal inlet 11 and the liquefied residue inlet 12, and react the pulverized coal with the liquefied residue The mass ratio of the mixture is 1:0.4, and the mixed materials rely on gravity to pass through the low-temperature dry distillation section and the high-temperature dry distillation section of the fast pyrolysis furnace in turn; among them, the temperature of the low-temperature dry distillation section is 550-580°C, and the temperature of the high-temperature dry distillation section is 800- 850℃; in the low-temperature dry distillation section, the liquefied residue is basically completely pyrolyzed, while the coal powder undergoes ...
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