Method and system for coupling power plant power generation and clean coal production
A power plant, clean technology, applied in steam generation method using heat carrier, lighting and heating equipment, fuel, etc., to achieve the effect of reducing pollutant emission, simplifying production process and stabilizing furnace temperature
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Embodiment 1
[0063] (1) put 5000Nm 3 / h of the first flue gas (900°C) indirectly heats 4,500kg of raw coal (lignite, with a particle size of 20mm) in the rotary kiln for 45 minutes of coal conversion, and the final conversion temperature is 600°C to obtain the first flue gas, the first pyrolysis gas and converted coal;
[0064] (2) put 5000Nm 3 / h of the second flue gas (900°C) indirectly heats the converted coal in the rotary kiln to remove impurities for 35 minutes. ;
[0065] (3) dry-cooling the de-miscellaneous coal to obtain clean coal;
[0066] (4) The first and second pyrolysis gases are merged into return air (temperature 450°C), and returned to the burner of the power plant boiler through the induced draft device for power generation; the first and second flue gas are merged into return flue gas ( 800℃) into the power plant boiler for power generation; the total flow of return air and return flue gas is 12000Nm 3 / h;
[0067] The total flow rate of the first flue gas and the...
Embodiment 2
[0070] (1) Use 6500Nm 3 / h of the first flue gas (1000°C) indirectly heats 4000kg of raw coal (non-caking coal, particle size: 30mm) in the tower moving bed to carry out coal conversion for 30min, and the final conversion temperature is 500°C to obtain the first flue gas, first pyrolysis gas and converted coal;
[0071] (2) Use 3500Nm 3 / h of the second flue gas (1000°C) indirectly heats the converted coal in the rotary kiln to remove impurities for 30 minutes, and the final removal temperature is 700°C to obtain the second flue gas, the second pyrolysis gas and the coal;
[0072] (3) dry-cooling the de-miscellaneous coal to obtain clean coal;
[0073] (4) The first and second pyrolysis gases are merged into return air (temperature 350°C), and returned to the burner of the power plant boiler through the induced draft device for power generation; the first and second flue gas are merged into return flue gas ( 900℃) into the power plant boiler for power generation; the total...
Embodiment 3
[0077] (1) Use 6000Nm 3 / h of the first flue gas (950°C) indirectly heats 5000kg of raw coal (long-flame coal, particle size: 3mm) in the tower-type moving bed, and carries out coal conversion for 40min, and the final conversion temperature is 550°C, and the first flue gas, first pyrolysis gas and converted coal;
[0078] (2) with 4000Nm 3 The first flue gas (950°C) in the rotary kiln indirectly heats the converted coal in the rotary kiln for 30 minutes of coal removal, and the final removal temperature is 650°C to obtain the second flue gas, the second pyrolysis gas and the removal of impurities coal;
[0079] (3) dry-cooling the de-miscellaneous coal to obtain clean coal;
[0080] (4) The first and second pyrolysis gases are merged into return air (temperature 400°C), and returned to the burner of the power plant boiler through the induced draft device for power generation; the first and second flue gas are merged into return flue gas ( 750℃) into the power plant boiler fo...
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