Ultralow emission treatment system and method for coke oven flue gas
A technology of flue gas and coke oven, which is applied in the field of coking, can solve the problems of reduced heat transfer efficiency, white smoke trailing, affecting production stability and safety, etc., to improve operational stability and efficiency, and eliminate the impact of waste heat boilers , Elimination of secondary waste problems
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Embodiment 1
[0051] A coking plant has a 1.3 million tons / year coke oven with a flue gas volume of 270,000 Nm 3 / hr, the original flue gas temperature is 260°C, where SO 2 =100mg / Nm 3 , NO x =1000mg / Nm 3 , soot=50mg / Nm 3 , apply the coke oven flue gas ultra-low emission treatment system of this embodiment to treat the coke oven flue gas.
[0052] Such as figure 1 As shown, the coke oven flue gas ultra-low emission control system of this embodiment includes a wet desulfurization device 100, a denitrification device 200, a waste heat boiler 300, an induced draft fan 400 and a chimney 500, and also includes an oil-medium heat exchanger 600 and a water-medium exchanger. Heater 700. From the coke oven raw flue gas to the ultra-clean flue gas, through the flue, the cooling section 601 of the oil-coal heat exchanger 600, the wet desulfurization device 100, and the reheating section 702 of the water-medium heat exchanger 700 are connected in sequence , the reheating section 602 of the oil-m...
Embodiment 2
[0066] A coking plant has a 1 million tons / year coke oven with a flue gas volume of 210,000 Nm 3 / hr, the original flue gas temperature is 230°C, where SO 2 =80mg / Nm 3 , NO x =800mg / Nm 3 , soot=100mg / Nm 3 , after applying the same coke oven flue gas ultra-low emission purification and waste heat utilization coupling treatment system and method as in Example 1, the ultra-clean flue gas temperature is 110 °C, NO x Content 25.5mg / Nm 3 , SO 2 Content 3.2mg / Nm 3 , dust 4.8mg / Nm 3 , the by-product steam of 0.5Mpa is 7.5 tons / hr, and there is no phenomenon of white smoke trailing.
Embodiment 3
[0068] A coking plant has a 1.7 million tons / year coke oven with a flue gas volume of 350,000 Nm 3 / hr, the original flue gas temperature is 280°C, where SO 2 =66mg / Nm 3 , NO x =1000mg / Nm 3 , soot=70mg / Nm 3 , using the coke flue gas ultra-low emission purification and waste heat utilization coupling treatment system roughly the same as in Example 1, the catalyst is a honeycomb catalyst, the honeycomb holes are square holes, and the pore diameter is 5mm; the oil-medium heat exchanger 600 and the water-medium heat exchange The device 700 uses finned heat exchange tubes, the pitch of the fins is 2.6mm, the height of the fins is 35mm, and the outer diameter of the heat exchange tubes is 32mm; x Content 25.5mg / Nm 3 , SO 2 Content 3.2mg / Nm 3 , dust 4.1mg / Nm 3 , the by-product steam of 0.5Mpa is 18 tons / hr, and there is no phenomenon of white smoke trailing.
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