Method for producing ultralow phosphoretic steel through carrying out CAS-OB molten steel ladle refining on premelting calcium ferrite
An extra-furnace refining and ultra-low phosphorus steel technology, which is applied in the metallurgical field, can solve the problems of insufficient utilization of converter productivity, reduction of scrap steel, long smelting time, etc., achieve dephosphorization efficiency and stability, reduce oxygen consumption, and reduce smelting The effect of intensity
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Embodiment 1
[0033] After the converter smelting is completed, the phosphorus content at the end of the converter is controlled below 0.03%, the tapping temperature is controlled at about 1590°C, the molten steel is not deoxidized during the tapping process, and slag blocking treatment is used during the tapping process; The ladle is transported to the CAS-OB refining station, and the molten steel is blown and stirred with argon. The flow rate of argon is controlled at 50NL / min, and the pre-melted calcium ferrite is added to the molten steel at one time from the silo. The dosage is controlled at 5Kg / ton of steel, the particle size is controlled at 0.1mm-100mm, and the refining treatment time is controlled at 12-15min. After the refining treatment, the argon stirring is stopped, and the ladle is opened out of the CAS-OB refining station; the ladle is transported to slag removal At the station, use the slag remover to remove the slag on the surface of the molten steel after dephosphorization,...
Embodiment 2
[0035]After the converter smelting is completed, the phosphorus content at the end of the converter is controlled below 0.03%, the tapping temperature is controlled at about 1620°C, the molten steel is not deoxidized during the tapping process, and slag blocking treatment is used during the tapping process; The ladle is transported to the CAS-OB refining station, and the molten steel is blown and stirred with argon. The flow rate of the argon gas is controlled at 100NL / min. The dosage is controlled at 8Kg / ton of steel, the particle size is controlled at 0.1mm-100mm, the refining treatment time is controlled at 9-12min, and the argon gas stirring is stopped after the refining treatment is completed, and the ladle is taken out of the CAS-OB refining station; the ladle is transported to the slag removal station At the station, use the slag remover to remove the slag on the surface of the molten steel after dephosphorization treatment, and then add a ladle covering agent of 4Kg / ton...
Embodiment 3
[0037] After the converter smelting is completed, the phosphorus content at the end of the converter is controlled below 0.03%, the tapping temperature is controlled at about 1650°C, the molten steel is not deoxidized during the tapping process, and slag blocking treatment is used during the tapping process; The ladle is transported to the CAS-OB refining station, and the molten steel is blown and stirred with argon. The flow rate of the argon gas is controlled at 180NL / min. The dosage is controlled at 10Kg / ton of steel, the particle size is controlled at 0.1mm-100mm, and the refining treatment time is controlled at 7-9 minutes. After the refining treatment, the argon stirring is stopped, and the ladle is opened out of the CAS-OB refining station; the ladle is transported to the slag removal station. At the station, use the slag removal machine to remove the slag on the surface of the molten steel after dephosphorization treatment, and then add a ladle covering agent of 5Kg / ton...
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