Production method of high-cleanliness sulfur-containing and aluminum-containing steel
A technology with high cleanliness and production method, applied in the field of alloy steel, can solve the problems of difficulty in ensuring the secondary oxidation of molten steel with low oxygen content, low level of quality control of molten steel smelting, and inability to meet the requirements of product use, so as to avoid polluting molten steel. The effect of reducing the unevenness of the composition, reducing the labor intensity, and reducing the cost of the production process
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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 and double-blowing converters for blowing, and the end point of molten steel is w ([S])=0.035%~0.045%, when the converter is tapping 0t~10t, add 2.0kg / t~3.0kg / t ordinary ferrosilicon alloy for preliminary deoxidation. When the tapping progress is 60%~80%, add 1.3kg / t~1.7kg / t aluminum block for deep deoxidation. 6.0kg / t~7.0kg / t lime and 2.5kg / t~3.0kg / t pre-melted refining slag are added near the end of tapping. Refined to the station w ([Al]) = 0.015% to 0.020%.
[0031] 2) The LF refining process does not add lime, refining slag and other slag materials, and uses aluminum particles and high-purity silicon carbide for diffusion deoxidation on the slag surface and precipitation deoxidation of aluminum ...
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 and double-blowing converters for blowing, and the end point of molten steel is w ([S])=0.035%~0.050%, when the converter is tapping 0t~10t, add 3.5kg / t~5.0kg / t ordinary ferrosilicon alloy for preliminary deoxidation. When the tapping progress is 60%~80%, add 0.9kg / t~1.5kg / t aluminum block for deep deoxidation. 6.0kg / t~7.0kg / t lime and 2.8kg / t~3.5kg / t pre-melted refining slag are added at the end of tapping. 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, and uses aluminum particles and high-purity silicon carbide for diffusion deoxidation on the slag surface and precipitation deoxidation of aluminum particle...
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 and double-blowing converters for blowing, and the end point of molten steel is w ([S])=0.030%~0.045%, when the converter is tapping 0t~10t, add 2.5kg / t~3.5kg / t ordinary ferrosilicon alloy for preliminary deoxidation. When the tapping progress is 60%~80%, add 1.1kg / t~1.6kg / t aluminum block for deep deoxidation. 6.0kg / t~7.0kg / t lime and 3.0kg / t~4.0kg / t pre-melted refining slag are added at the end of tapping. 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, and uses aluminum particles and high-purity silicon carbide for diffusion deoxidation on the slag surface and precipitation deoxidation of aluminum particl...
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