Refining method of reducing slag made by CAS refining furnace for desulfurization
A refining furnace and converter technology, applied in the field of metallurgical steelmaking, can solve the problems of no desulfurization function, molten steel returning to the furnace, affecting the production rhythm and economic benefits of the enterprise, etc., to achieve the effect of broadening the refining function, avoiding sulfur return, and having desulfurization ability.
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Embodiment 1
[0021] Example 1: 115t of molten steel is tapped from the converter, and the sulfur content at the end point of the molten steel is 0.028%. During the tapping process, lime is added to the ladle at a ratio of 3kg / t, and aluminum, magnesium and calcium are added to the ladle at a ratio of 3kg / t. The tapping process is carried out at the bottom of the ladle. Argon blowing and stirring, the flow rate is 18M 3 / h, time 2 minutes. After entering CAS, take samples to measure temperature and determine oxygen OXP=25ppm, control molten steel temperature at 1600-1630°C, add calcium carbide in three batches according to 0.8Kg / t ratio according to slag color, and divide into three batches according to 0.5Kg / t ratio according to steel slag fluidity Add Fluorite in batches. After 20 minutes of lowering the hood and stirring weakly for 5 minutes, the oxygen was fixed at OXP=4.5ppm, and the sulfur content in the tapped steel was 0.021%.
Embodiment 2
[0022] Embodiment 2: Converter tapping 115t molten steel, the final sulfur content of molten steel is 0.021%, during the tapping process, add lime to the ladle according to the ratio of 3.5kg / t, add aluminum, magnesium and calcium to the ladle according to the ratio of 2kg / t, and carry out the ladle process during the tapping process. Bottom blowing argon stirring, flow rate 20M 3 / h, time 1.5 minutes. After entering CAS, take samples to measure temperature and determine oxygen OXP=23ppm, control the temperature of molten steel at 1600-1630°C, add calcium carbide in two batches according to the ratio of 0.7Kg / t according to the color of slag, and divide it into two batches according to the ratio of 0.4Kg / t according to the fluidity of steel slag Add Fluorite in batches. After 18 minutes of lowering the hood and stirring weakly for 5 minutes, the oxygen was fixed at OXP=3.8ppm, and the sulfur content of the steel was 0.016%.
Embodiment 3
[0023] Embodiment 3: Converter tapping 115t molten steel, the end point sulfur content of molten steel is 0.022%, during the tapping process, add lime to the ladle according to the ratio of 3.2kg / t, add aluminum magnesium calcium to the ladle according to the ratio of 1.5kg / t, the tapping process is carried out Argon blowing and stirring at the bottom of the ladle, the flow rate is 19M 3 / h, time 1.8 minutes. After entering CAS, take samples to measure temperature and determine oxygen OXP=24ppm, control the temperature of molten steel at 1600-1630°C, add calcium carbide at a ratio of 0.5Kg / t according to the color of slag, and add fluorite at a ratio of 0.3Kg / t according to the fluidity of steel slag. After 19 minutes of lowering the hood and stirring weakly for 5 minutes, the oxygen was fixed at OXP=3.5ppm, and the sulfur content in the tapped steel was 0.019%.
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