A method for smelting low-nitrogen boron-containing steel to increase the yield of boron element
A smelting method and a yield technology, applied in the field of low nitrogen boron-containing steel smelting, can solve the problems of increased production cost, complicated process route, etc., and achieve the effects of reducing oxidation, improving yield and reducing oxidizability
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Embodiment 1
[0024] (1) Boiling tapping at the end of the converter, the slag is controlled during the tapping process, 1.2kg / t of slag adjusting agent and 2.3kg / t of lime are added to the slag surface after tapping, argon is blown at the bottom of the ladle during the tapping process, and the bottom of the ladle is blown The flow rate is 80NL / min, keeping the molten steel agitated, but not splashing.
[0025] (2) The ladle is hoisted to the RH station. The oxygen content of the RH station is 0.0435%, and the T.Fe+MnO is 9.65%. After the ladle is lifted in place, it is vacuumed and decarburized. The vacuum degree is controlled below 2mbar, and the decarburization takes 12.5min After decarburization, the oxygen content of the molten steel is 0.0185%, and then add metal aluminum, ferrosilicon, low-carbon ferromanganese, carbon powder, etc. The particle size is 30-60mm, and the composition of the slagging agent is: 20%≤Al≤45%, 5%≤Ca≤15%, 20%≤CaO≤30%, 10%≤Al 2 o 3 ≤15%, 5%≤CaF 2 ≤10%, and o...
Embodiment 2
[0028] (1) Converter tapping is boiling tapping, and the slag is controlled during the tapping process. After tapping, 2.9kg / t of slag adjusting agent and 3.3kg / t of lime are added to the slag surface. The blowing flow rate is 180NL / min to keep the molten steel agitated, but not toss and splash.
[0029] (2) The ladle is hoisted to the RH station. The oxygen content of the RH station is 0.035%, and the T.Fe+MnO is 7.58%. After the ladle is lifted in place, it is vacuumed and decarburized. The vacuum degree is controlled below 2mbar, and the decarburization takes 11.8min After decarburization, the oxygen content of the molten steel is 0.0083%, and then add metal aluminum, ferrosilicon, low-carbon ferromanganese, carbon powder, etc. The particle size is 30-60mm, and the composition of the slagging agent is: 20%≤Al≤45%, 5%≤Ca≤15%, 20%≤CaO≤30%, 10%≤Al 2 o 3 ≤15%, 5%≤CaF 2 ≤10%, and other unavoidable impurities, circulate for 6.5min, molten steel T.O is 0.0014%, slag T.Fe+MnO is...
Embodiment 3
[0032] (1) Converter tapping is boiling tapping, and the slag is controlled during the tapping process. After tapping, 2.3kg / t of slagging agent and 2.5kg / t of lime are added to the slag surface. Argon is blown at the bottom of the ladle during the tapping process. The blowing flow rate is 120NL / min to keep the molten steel agitated, but not toss and splash.
[0033](2) The ladle is hoisted to the RH station. The oxygen content of the RH station is 0.0380%, and the T.Fe+MnO is 8.62%. After the ladle is lifted in place, it is vacuumed and decarburized. The vacuum degree is controlled below 2mbar, and the decarburization takes 12.3min After decarburization, the oxygen content of the molten steel is 0.0124%, and then add metal aluminum, ferrosilicon, low-carbon ferromanganese, carbon powder, etc. The particle size is 30-60mm, and the composition of the slagging agent is: 20%≤Al≤45%, 5%≤Ca≤15%, 20%≤CaO≤30%, 10%≤Al 2 o 3 ≤15%, 5%≤CaF 2 ≤10%, and other unavoidable impurities, cir...
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