Smelting method of low-cost high-purity 60Si2Mn spring steel
A smelting method and spring steel technology, applied in the field of alloy steel smelting, can solve the problems of high production cost, low molten steel cleanliness, and many process routes, and achieve the effects of reducing production and manufacturing costs, ensuring molten steel purity, and simple production process
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[0035] Example 1
[0036] 1) Use w ([S])= 0.030% molten iron and ordinary steel scrap as raw materials, using top-bottom combined blowing converter smelting, tapping volume 25t ~ 35t, adding 0.5kg / t of 99.9% purity aluminum cake for molten steel precipitation deoxidation; adding aluminum cake for deoxidation After the end, use ordinary recarburizers, ordinary ferrosilicon alloy, silicomanganese, high-carbon ferromanganese, and ferrochrome for preliminary alloying of molten steel; after alloying, before the end of molten steel tapping, add lime and refined slag each at 6.5kg / t.
[0037] Early refining slag w (CaO) / w (SiO 2 )=5.5, w (Al 2 O 3 )= 25.3%; refined to the station w ([Al])=0.019%.
[0038] 2) In the process of molten steel refining, the bottom blowing and stirring argon flow rate is 400 NL / min~600NL / min during the early heating stage, the bottom blowing and stirring argon gas flow rate is 200 NL / min~300NL / min when the temperature rises in the middle of refining, and the b...
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[0043] Example 2
[0044] 1) Use w ([S])= 0.020% molten iron and ordinary steel scrap as raw materials, using top-bottom combined blowing converter smelting, tapping volume 25t-30t, adding 0.8kg / t aluminum cake with a purity of 99.9% for molten steel precipitation deoxidation; adding aluminum cake for deoxidation After the completion, use common recarburizers, common ferrosilicon alloy, silicomanganese, high-carbon ferromanganese, and ferrochrome for preliminary alloying of molten steel; after alloying, before molten steel tapping, add 5.5kg / t of lime and refined slag each .
[0045] Early refining slag w (CaO) / w (SiO 2 )=4.9, w (Al 2 O 3 )= 24.6%; refined to the station w ([Al])=0.029%.
[0046] 2) In the process of molten steel refining, the bottom blowing and stirring argon flow rate is 300 NL / min~450NL / min in the early heating stage, the bottom blowing and stirring argon gas flow rate is 150 NL / min~250NL / min when the temperature rises in the middle of refining, and the bottom b...
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[0051] Example 3
[0052] 1) Use w ([S])= 0.025% molten iron and ordinary steel scrap as raw materials, using top-bottom combined blowing converter smelting, tapping volume 35t-40t, adding 1.0kg / t aluminum cake with a purity of 99.9% for molten steel precipitation deoxidation; adding aluminum cake for deoxidation After the completion, use common recarburizers, common ferrosilicon alloy, silicomanganese, high-carbon ferromanganese, and ferrochrome for preliminary alloying of molten steel; after alloying, before molten steel tapping, add lime and refined slag each 5.0kg / t .
[0053] Early refining slag w (CaO) / w (SiO 2 )=4.2, w (Al 2 O 3 )= 26.5%; refined to the station w ([Al])=0.035%.
[0054] 2) In the process of molten steel refining, the bottom blowing and stirring argon flow rate is 450 NL / min~500NL / min during the early heating stage, the bottom blowing and stirring argon gas flow rate is 200 NL / min~300NL / min when the temperature rises in the middle of refining, and the bottom ...
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