Oxygen blast furnace and gas-based shaft furnace joint production system and joint production method
A gas-based shaft furnace and combined production technology, applied in the field of metallurgy, can solve the problems of high cost, limitation, singleness, etc., and achieve the effect of eliminating high energy consumption and solving the insufficient circulation of oxygen blast furnace top gas
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Embodiment 1
[0091] refer to figure 1 and 2 , the joint production system and method of oxygen blast furnace and gas-based shaft furnace are as follows:
[0092] 1) The blast furnace top gas of the oxygen blast furnace 10 is dedusted by the dedusting device 30 and is divided into two parts. The first part of gas enters the water gas shift device 40 to generate H 2 , then enter the CO 2 The removal device 50, the second part of the gas directly enters the CO2 The removal device 50 removes part of the CO after mixing the two parts of the gas with the top gas of the gas-based shaft furnace 2 , after being pressurized by the pressurizer 60, it enters the gasifier 70 and reacts with oxygen and coal powder to obtain H 2 / CO=1~2:1 High-temperature reducing gas, part of which is blown into the oxygen blast furnace 10 from the upper and lower air inlets of the oxygen blast furnace, and the other part enters the gas-based shaft furnace 20 to reduce and oxidize pellets to produce sponge iron.
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Embodiment 2
[0111] Basically the same as Example 1, the difference is:
[0112] According to theoretical calculation, 3000m 3 Oxygen blast furnace production technical indicators are as follows:
[0113] Oxygen consumption of oxygen blast furnace (90% purity): 245Nm 3 / tHM
[0114] Oxygen blast furnace coal ratio: 200kg / tHM
[0115] Oxygen blast furnace coke ratio: 178kg / tHM
[0116] Furnace top gas volume: 1357Nm 3 / tHM
[0117] Top gas composition: CO: 50.4%, CO 2 : 36.9%, H 2 : 6.3%, H 2 O: 2.6%, N 2 : 3.8%
[0118] Oxygen blast furnace output: 12600tHM / d
[0119] Gasifier oxygen consumption (90% purity): 162Nm 3 / tHM
[0120] Gasifier pulverized coal consumption: 225kg / tHM
[0121] Composition of circulating gas: CO: 45.8%, H 2 : 48.4%, N 2 : 5.8%
[0122] Circulating gas temperature: 1100°C
[0123] Circulating gas volume at the upper air outlet: 382Nm 3 / tHM
[0124] Circulating gas volume at the lower air outlet: 400Nm 3 / tHM
[0125] Gas-based shaft furnace o...
Embodiment 3
[0127] Basically the same as Example 1, the difference is:
[0128] According to theoretical calculation, 5000m 3 Oxygen blast furnace production technical indicators are as follows:
[0129] Oxygen consumption of oxygen blast furnace (95% purity): 225Nm 3 / tHM
[0130] Oxygen blast furnace coal ratio: 200kg / tHM
[0131] Oxygen blast furnace coke ratio: 191kg / tHM
[0132] Furnace top gas volume: 1368Nm 3 / tHM
[0133] Top gas composition: CO: 51.8%, CO 2 : 37.5%, H 2 : 6.6%, H 2 O: 2.6%, N 2 : 1.5%
[0134] Oxygen blast furnace output: 21000tHM / d
[0135] Gasifier oxygen consumption (95% purity): 133Nm 3 / tHM
[0136] Gasifier pulverized coal consumption: 200kg / tHM
[0137] Composition of circulating gas: CO: 47.8%, H 2 : 49.0%, N 2 : 3.2%
[0138] Circulating gas temperature: 900°C
[0139] Circulating gas volume at the upper air outlet: 382Nm 3 / tHM
[0140] Circulating gas volume at the lower air outlet: 400Nm 3 / tHM
[0141] Gas-based shaft furnace ou...
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