System and method for utilizing top gas of sponge iron produced by reducing shaft furnace
A technology of top gas and sponge iron, which is applied in shaft furnaces, furnaces, furnace types, etc., can solve the problems of complex top gas treatment process and low heat energy recovery rate of top gas, and achieve low-carbon and environmental protection production, Effect of Reducing Energy Consumption of Shaft Furnace
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Embodiment 1
[0052] In this embodiment, coke oven gas is used as the raw material gas to reduce the iron ore in the shaft furnace, and the composition of the coke oven gas after refining and desulfurization is: 60% H 2 , 8% CO, 27% CH 4 , 4%C 2+ , 2%CO 2 , 2%N 2 , 0.5% O 2 . 350-400 ℃ shaft furnace top gas composition: 32.6%H 2 , 12.2% CO, 12.6% CH 4 , 9.7%CO 2 , 9.3%N 2 , 23.6%H 2 O, after being discharged through the exhaust pipe, it directly enters the iron concentrate pellet preheating tank to preheat the iron concentrate pellet. Such as figure 1 As shown, the outlet temperature of the gas is 150°C after passing through the charge preheating tank 2, and then enters the cooling and dust removal system such as the washing tower 4 to cool down to about 40°C, and the dust content drops to 500mg / m 3 . The dedusted gas is dehydrated by the dehydrator 5, and then pressurized by the compressor 7 and then enters the decarbonization system 6 such as MDEA solution for decarburization ...
Embodiment 2
[0057] In this embodiment, coke oven gas is used as the raw material gas to reduce the iron ore in the shaft furnace, and the composition of the coke oven gas after refining and desulfurization is: 60% H 2 , 8% CO, 27% CH 4 , 4%C 2+ , 2%CO 2 , 2%N 2 , 0.5% O 2 . 350-400 ℃ shaft furnace top gas composition: 32.6%H 2 , 12.2% CO, 12.6% CH 4 , 9.7%CO 2 , 9.3%N 2 , 23.6%H 2 O, after being discharged through the exhaust pipe, it directly enters the iron concentrate pellet preheating tank to preheat the iron concentrate pellet. Such as figure 1 As shown, the outlet temperature of the gas is 150°C after passing through the charge preheating tank 2, and then enters the cooling and dust removal system such as the washing tower 4 to cool down to about 40°C, and the dust content drops to 500mg / m3. The dedusted gas is dehydrated by the dehydrator 5, and then pressurized by the compressor 7 and then enters the decarbonization system 6 such as MDEA solution for decarburization tre...
Embodiment 3
[0062] In this embodiment, coke oven gas is used as the raw material gas to reduce the iron ore in the shaft furnace, and the composition of the coke oven gas after refining and desulfurization is: 60% H 2 , 8% CO, 27% CH 4 , 4%C 2+ , 2%CO 2 , 2%N 2 , 0.5% O 2 . 350-400 ℃ shaft furnace top gas composition: 32.6%H 2 , 12.2% CO, 12.6% CH 4 , 9.7%CO 2 , 9.3% N 2 , 23.6%H 2 O, after being discharged through the exhaust pipe, it directly enters the iron concentrate pellet preheating tank to preheat the iron concentrate pellet. Such as figure 1As shown, the outlet temperature of the gas is 150°C after passing through the charge preheating tank 2, and then enters the cooling and dust removal system such as the washing tower 4 to cool down to about 40°C, and the dust content drops to 500mg / m3. The dedusted gas is dehydrated by the dehydrator 5, and then pressurized by the compressor 7 and enters the decarbonization system 6 such as MDEA solution for decarburization treatmen...
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