Carbonaceous material pyrolysis system and pyrolysis process thereof
A carbonaceous material and pyrolysis technology, which is applied to the endothermic pyrolysis system and its process field, and can solve the problems of pyrolysis gas back-mixing, pressure fluctuation, etc.
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Embodiment 1
[0055] use image 3 The pyrolysis system and process of the present invention shown pyrolyze lignite coal whose coal quality analysis data are shown in Table 1 below.
[0056] Table 1
[0057]
[0058] The process scale of this example is 1 million tons / year (3500 tons / day), and the raw coal S1 feed rate is 145 tons / hour.
[0059] 1) After the raw coal S1 is crushed to ≤50mm, it enters the drying device 1 and is heated to about 200°C to remove most of the moisture. After drying, the moisture content of the coal is about 5%;
[0060] 2) The dry tail gas S5 from the drying device 1 has a temperature of about 110°C. After being dedusted by the gas-solid separator 11, about 70% is used as the circulating tail gas S8, and the rest S13 is discharged into the atmosphere after desulfurization and other treatments; the circulating tail gas S8 is mixed with the waste heat gas S17 from the solid medium heater 6 to about 300°C, and enters the drying device 1 as the drying medium S21;...
Embodiment 2
[0069] use image 3 The pyrolysis system and process of the present invention shown pyrolyzes long flame coal whose coal quality analysis data are shown in Table 2 below.
[0070] Table 2
[0071]
[0072]
[0073] The process scale of this example is 1 million tons / year (3500 tons / day), and the raw coal S1 feed rate is 145 tons / hour.
[0074] 1) After the raw coal S1 is crushed to ≤50mm, it enters the drying device 1 and is heated to about 180°C to remove most of the moisture. After drying, the moisture content of the coal is about 1%;
[0075] 2) The dry tail gas S5 from the drying device 1 has a temperature of about 110°C. After being dedusted by the gas-solid separator 11, about 50% is used as the circulating tail gas S8, and the remaining part S13 is discharged into the atmosphere after desulfurization and other treatments; the circulating tail gas S8 is mixed with the waste heat gas S17 from the burner 6 to about 300°C, and enters the drying device 1 as the dryin...
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Abstract
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