Dephosphorization control method for unequal samples at converter smelting end points of DC04 steel
A converter smelting and control method technology, which is applied in the field of converter steelmaking, can solve the problems of heat loss, shortening smelting cycle, temperature reduction, etc., and achieves the advantages of reducing refractory material and energy consumption, increasing the oxidizing atmosphere in the furnace, and improving the production operation rate. Effect
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Embodiment 1
[0022] A kind of dephosphorization control method of DC04 steel converter smelting end point of the present embodiment is not equal, comprising the following steps:
[0023] S1: On the basis of the optimal amount of slag remaining and slag basicity, the optimum amount of slag remaining for smelting DC04 steel in a 300-ton converter is 17 to 24 tons and the slag basicity is 4.3-4.7. If the amount of slag remaining is too low, it will affect the The dephosphorization effect makes the phosphorus content of the molten steel at the end point higher; while the amount of slag left is too high, the slag layer will be too thick, and the temperature rise in the auxiliary blowing process will be slow, which will affect the temperature of the molten steel at the end point, resulting in insufficient temperature of the molten steel at the end point. If the slag alkalinity is too low, it is not conducive to the dephosphorization reaction; if the slag alkalinity is too high, the fluidity of th...
Embodiment 2
[0031] The dephosphorization control method of a DC04 steel converter with different smelting end points in this embodiment is basically the same as in Example 1, the difference is that in this embodiment, the 300-ton converter has confirmed that the bottom blowing condition of the converter is good, and the converter is continuous. For production, the average carbon and oxygen product of the first three furnaces is calculated to be 14.3. After the steel is tapped from the previous furnace, the amount of slag remaining after slag turning is controlled at 24 tons. The furnace is protected by slag splashing. The slag alkalinity is set to 4.7, and the static model is calculated. 38.7 tons of scrap steel, 294.2 tons of molten iron, of which the molten iron includes the following chemical components in mass percentages: C: 4.57%, Si: 0.60%, Mn: 0.18%, P: 0.141%, S: 0.002%, V: 0.064%, Ti : 0.123%, the rest is Fe and other impurities. The temperature of molten iron after KR treatment...
Embodiment 3
[0034] The dephosphorization control method of a DC04 steel converter with different smelting end points in this embodiment is basically the same as in Embodiment 1, the difference is that in this embodiment, the 300-ton converter in this embodiment confirms the converter bottom blowing condition Good, the converter is in continuous production, the average carbon and oxygen product of the first 3 furnaces is calculated as 13.6, the steel is tapped from the previous furnace, the amount of slag left after slag turning is controlled at 20 tons, the furnace is protected by slag splashing, the slag basicity is set to 4.5, and static Model calculations add 25.5 tons of steel scrap and 294.2 tons of molten iron, where the molten iron includes the following chemical components in mass percentages: C: 4.59%, Si: 0.39%, Mn: 0.16%, P: 0.141%, S: 0.001%, V: 0.055%, Ti: 0.058%, and the rest are Fe and other impurities. After the molten iron is KR treated, the temperature is 1273°C, and sme...
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