Method for controlling nitrogen content in Al deoxidization steel by converter process
An aluminum deoxidizing steel nitrogen and converter technology, applied in the field of iron and steel metallurgy, can solve problems such as nitrogen increase, and achieve the effect of reducing the nitrogen content of the slab and preventing nitrogen increase
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Embodiment 1
[0038] The experimental conditions are:
[0039] (1) Nominal 120t top and bottom double blowing converter, after blowing for 10min, the bottom blowing gas is changed from N 2 Converted to Ar gas, the production steel grade is P510L, and the production process flow is LD-LF-CC.
[0040] (2) When the converter is charged, the amount of scrap steel added is 75kg / t steel.
[0041] (3) Using active lime (containing CaO85.0~95.0% by weight, 5%≥MgO>0, 2.5%≥SiO 2 >0, the rest are burn reduction and Al 2 O 3 , P, S and other trace impurities) slag, when the converter starts slagging, the basicity of the converter slag CaO / SiO 2 Control at 5.
[0042] (4) The slag added at the beginning of tapping contains by weight: CaO: 72.2%, SiO 2 : 2.7%, Al 2 O 3 : 3.2%, Na 2 O: 2.8%, CaF 2 : 11.6%, MgO: 3.5%, N: 0.02%, and the rest are trace impurities such as burning and P, S, etc., the addition amount is 7kg / t steel; after adding the slag, add aluminum and other alloys.
[0043] (5) T...
Embodiment 2
[0047] The experimental conditions are:
[0048] (1) Nominal 120t top and bottom double blowing converter, after blowing for 10min, the bottom blowing gas is changed from N 2 Converted to Ar gas, the production steel grade is P510L, and the production process flow is LD-LF-CC.
[0049] (2) When the converter is charged, the amount of scrap steel added is 60kg / t steel.
[0050] (3) Using active lime (containing CaO85.0~95.0% by weight, 5%≥MgO>0, 2.5%≥SiO 2 >0, the rest are burn reduction and Al 2 O 3 , P, S and other trace impurities) slag, when the converter starts slagging, the basicity of the converter slag CaO / SiO 2 Control at 6.
[0051] (4) The slag added at the beginning of tapping contains by weight: CaO: 74.6%, SiO 2 : 1.8%, Al 2 O 3 : 2.6%, Na 2 O: 2.7%, CaF 2 : 9.4%, MgO: 4.4%, N: 0.03%, and the rest are ignition reduction and trace impurities such as P and S. The addition amount is 8kg / t steel; after adding slag, add aluminum and other alloys.
[0052] (5...
Embodiment 3
[0065] The experimental conditions are:
[0066] (1) Nominal 120t top and bottom double blowing converter, after blowing for 10min, the bottom blowing gas is changed from N 2 Converted to Ar gas, the production steel grade is 20CrMoH, and the production process flow is LD—LF—RH—BCC.
[0067] (2) When the converter is charged, the amount of scrap steel added is 0kg / t steel.
[0068] (3) Using active lime (containing CaO85.0~95.0% by weight, 5%≥MgO>0, 2.5%≥SiO 2 >0, the rest are burn reduction and Al 2 O 3 , P, S and other trace impurities) slag, when the converter starts slagging, the basicity of the converter slag CaO / SiO 2 Control at 7.
[0069] (4) The slag added at the beginning of tapping contains CaO: 73.3%, SiO by weight percentage 2 : 2.4%, Al 2 O 3 : 2.7%, Na 2 O: 2.8%, CaF 2: 10.5%, MgO: 4.0%, N: 0.03%, the rest are trace impurities such as burning and P, S, etc., the addition amount is 9kg / t steel; after adding the slag, add aluminum and other alloys.
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