Method for controlling phosphorus content of end point molten steel smelted by a top-bottom combined blowing converter to be less than 30 ppm
A converter smelting and control method technology, applied in the direction of manufacturing converters, improving process efficiency, etc., can solve the problem that it is difficult to reach the molten steel at the end of smelting, and achieve the effect of ensuring the fluctuation range
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Embodiment 1
[0021] Weigh 72.2kg / t of primary slag according to the amount of each ton of steel material (hot metal + scrap), of which active lime is 45.7kg / t, lightly burned dolomite is 11.4kg / t, and lightly burned magnesium balls are 6.2kg / t, sintering return ore is 4.2kg / t, slagging agent is 2.4kg / t, miscellaneous ash is 2.4kg / t; and the secondary total slag material with an amount of 44.6kg / t per ton of steel material, of which active lime is 27.5kg / t, 2.7kg / t for lightly burned dolomite, and 14.4kg / t for sintering and returning ore. In order to ensure the phosphorus content of the end point molten steel, the phosphorus content in the active lime is 0.005%, the phosphorus content of light-burned dolomite and light-burned magnesium ball slag is 0.027%, the phosphorus content in sintering and returning ore is 0.043%, slagging agent and The phosphorus content in miscellaneous ash is 0.030%.
[0022] Then proceed as follows:
[0023] (1) Low-phosphorus steel with a phosphorus content of...
Embodiment 2
[0033] Compared with Example 1, this example differs in that 30% of the oxidized slag remains in the furnace after tapping, the amount of smelting slag added, the primary slag pouring temperature, and the carbon content at the end point. In this example, 74.9kg / t of primary slag is added according to the amount of each ton of iron and steel material (hot metal + scrap steel), of which active lime is 35.1kg / t, lightly burned dolomite is 20.2kg / t, and lightly burned magnesium balls are 6.4kg / t, 13.2kg / tt for sintering and returning to ore; Return ore is 12.3kg / t. In this embodiment, the primary slagging temperature is controlled to be 1403° C., the carbon content of the molten steel at the end point of the converter is 0.04%, and the phosphorus content of the molten steel at the end point is 0.0028%.
Embodiment 3
[0035] Compared with Examples 1 and 2, this example differs in that 35% of the oxidized slag remains in the furnace after tapping, the amount of smelting slag added and the carbon content at the end point. In this example, 68.4kg / t of primary slag is weighed according to the amount of each ton of steel material (hot metal + scrap steel), of which active lime is 39.4kg / t, lightly burned dolomite is 13.2kg / t, and lightly burned magnesium balls are 6.3kg / t, sintering and returning 9.5kg / tt; and 66.5kg / t secondary total slag material per ton of steel material, of which active lime is 26.1kg / t and lightly burned dolomite is 11.3kg / t , 2.4kg / t for lightly burned magnesium balls, and 26.6kg / t for sintered ore return. In this embodiment, the temperature at the end point of the converter is 1640°C, the carbon content at the end point of the converter is 0.05%, and the phosphorus content in the molten steel at the end point is 0.0018%.
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