Joint production system and joint production method of oxygen blast furnace and gas-based shaft kiln
A gas-based shaft furnace and combined production technology, applied in the field of metallurgy, can solve the problems of limitation, high cost, singleness, etc., and achieve the effect of solving the insufficient circulation of oxygen blast furnace top gas and eliminating high energy consumption
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Embodiment 1
[0112] refer to figure 2 and 4 , the joint production system and method of oxygen blast furnace and gas-based shaft furnace are as follows:
[0113] 1) After the top gas of the oxygen blast furnace 10 is dedusted by the dedusting device 30, the gas is divided into two parts. The first part of blast furnace top gas enters the water gas shift device 40 to generate H 2 , then enter the first CO 2 The removal device 50, the second part of the gas directly enters the second CO 2 Removal device 80. The first part of the gas is pressurized and a certain amount of CO 2 And the shaft furnace top gas enters the gasifier 70, reacts chemically with oxygen and coal powder, and obtains H 2 The high-temperature reducing gas with / CO=1~2:1 is blown into the upper air inlet 13 of the blast furnace body, the lower air inlet 12 of the blast furnace hearth and the reducing gas inlet 21 of the gas-based shaft furnace respectively. The second part of the gas from the second CO 2 The remova...
Embodiment 2
[0132] Basically the same as Example 1, the difference is:
[0133] According to theoretical calculation, 3000m 3 Oxygen blast furnace production technical indicators are as follows:
[0134] Oxygen consumption of oxygen blast furnace (90% purity): 255Nm 3 / tHM
[0135] Oxygen blast furnace coal ratio: 200kg / tHM
[0136] Oxygen blast furnace coke ratio: 185kg / tHM
[0137] Furnace top gas volume: 1370Nm 3 / tHM
[0138] Top gas composition: CO: 48.7%, CO 2 : 37.2%, H 2 : 8.3%, H 2 O: 2.6%, N 2 : 3.4%
[0139] Oxygen blast furnace output: 12600tHM / d
[0140] Gasifier oxygen consumption (90% purity): 150Nm 3 / tHM
[0141] Gasifier pulverized coal consumption: 210kg / tHM
[0142] Composition of circulating gas: CO: 44.7%, H 2 : 49.5%, N 2 : 5.8%
[0143] Circulating gas temperature: 1100°C
[0144] Circulating gas volume at the upper air outlet: 390Nm 3 / tHM
[0145] Circulating gas volume at the lower air inlet: 410Nm 3 / tHM
[0146] Gas-based shaft furnace ou...
Embodiment 3
[0148] Basically the same as Example 1, the difference is:
[0149] According to theoretical calculation, 5000m 3 Oxygen blast furnace production technical indicators are as follows:
[0150] Oxygen consumption of oxygen blast furnace (95% purity): 230Nm 3 / tHM
[0151] Oxygen blast furnace coal ratio: 200kg / tHM
[0152] Oxygen blast furnace coke ratio: 195kg / tHM
[0153] Furnace top gas volume: 1390Nm 3 / tHM
[0154] Top gas composition: CO: 49.7%, CO 2 : 37.5%, H 2 : 8.7%, H 2 O: 2.6%, N 2 : 1.5%
[0155] Oxygen blast furnace output: 21000tHM / d
[0156] Gasifier oxygen consumption (95% purity): 130Nm 3 / tHM
[0157] Gasifier pulverized coal consumption: 190kg / tHM
[0158] Composition of circulating gas: CO: 46.7%, H 2 : 50.1%, N 2 : 3.2%
[0159] Circulating gas temperature: 900°C
[0160] Circulating gas volume at the upper air outlet: 380Nm 3 / tHM
[0161] Circulating gas volume at the lower air inlet: 400Nm 3 / tHM
[0162] Gas-based shaft furnace outpu...
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