A production method of high cleanliness sulfur-containing aluminum-containing steel
A technology with high cleanliness and production methods, applied in the field of alloy steel, can solve the problems that it is difficult to ensure the secondary oxidation of molten steel with low oxygen content, the quality control level of molten steel smelting is low, and the requirements for product use cannot be met, so as to avoid contamination of molten steel Inhomogeneity and composition, reduce labor intensity, reduce the effect of production process cost
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Embodiment 1
[0029] 20CrMnTi, in steel w ([Al]) =0.020%~0.040%, w ([S])=0.020%~0.037%, w ([Si]) =0.20%~0.30%,. It specifically includes the following steps:
[0030] 1) Use high-sulfur molten iron, slag steel and sulfur-containing scrap steel as raw materials, and use top-bottom blowing converter for blowing, and the molten steel ends. w ([S])=0.035%~0.045%, when the converter taps 0t~10t, add 2.0kg / t~3.0kg / t ordinary ferrosilicon alloy for preliminary deoxidation. When the tapping progress is 60%~80%, 1.3kg / t~1.7kg / t aluminum block is added for deep deoxidation. At the end of tapping, 6.0kg / t~7.0kg / t lime and 2.5kg / t~3.0kg / t premelting refining slag are added. Refined to the station w ([Al]) =0.015%~0.020%.
[0031] 2) The LF refining process does not add lime, refining slag and other slag materials. Aluminum particles and high-purity silicon carbide are used for slag surface diffusion deoxidation and aluminum particle precipitation deoxidation. The amount of high-purity silicon ca...
Embodiment 2
[0037] F45MnVS, in steel w ([Al]) =0.010%~0.040%, w ([S])=0.035%~0.075%, w ([Si]) =0.30%~0.60%,. It specifically includes the following steps:
[0038] 1) Use high-sulfur molten iron, slag steel and sulfur-containing scrap steel as raw materials, and use top-bottom blowing converter for blowing, and the molten steel ends. w ([S])=0.035%~0.050%, when the converter taps 0t~10t, add 3.5kg / t~5.0kg / t common ferrosilicon alloy for preliminary deoxidation. When the tapping progress is 60%~80%, 0.9kg / t~1.5kg / t aluminum block is added for deep deoxidation. At the end of tapping, 6.0kg / t~7.0kg / t lime and 2.8kg / t~3.5kg / t premelting refining slag are added. Refined to the station w ([Al]) =0.010%~0.020%.
[0039] 2) The LF refining process does not add lime, refining slag and other slag materials. Aluminum particles and high-purity silicon carbide are used for slag surface diffusion deoxidation and aluminum particle precipitation deoxidation. The amount of high-purity silicon carbi...
Embodiment 3
[0045] 42CrMo-S, in steel w ([Al]) =0.020%~0.045%, w ([S])=0.015%~0.030%, w ([Si]) =0.17%~0.37%,. It specifically includes the following steps:
[0046] 1) Use high-sulfur molten iron, slag steel and sulfur-containing scrap steel as raw materials, and use top-bottom blowing converter for blowing, and the molten steel ends. w ([S])=0.030%~0.045%, when the converter taps 0t~10t, add 2.5kg / t~3.5kg / t common ferrosilicon alloy for preliminary deoxidation. When the tapping progress is 60%~80%, 1.1kg / t~1.6kg / t aluminum block is added for deep deoxidation. At the end of tapping, 6.0kg / t~7.0kg / t lime and 3.0kg / t~4.0kg / t premelting refining slag are added. Refined to the station w ([Al]) =0.020%~0.030%.
[0047] 2) The LF refining process does not add lime, refining slag and other slag materials. Aluminum particles and high-purity silicon carbide are used for slag surface diffusion deoxidation and aluminum particle precipitation deoxidation. The amount of high-purity silicon carb...
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