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SWRCH22A冷锻钢100 t LF精炼造渣制度的分析和工艺优化
引用本文:高长益,张 毅,谢 祥,王琳松,郑家良,王 谦.SWRCH22A冷锻钢100 t LF精炼造渣制度的分析和工艺优化[J].特殊钢,2016,37(3):35-38.
作者姓名:高长益  张 毅  谢 祥  王琳松  郑家良  王 谦
作者单位:水城钢铁集团公司1技术中心; 2炼钢厂,六盘水553028; 3水城钢铁集团公司,六盘水553028; 4重庆大学材料科学与工程学院,重庆400044
摘    要:为减少钢中夹杂物和对夹杂物变性处理,防止连铸水口结瘤,对100 t LF 5炉SWRCH22A冷镦钢(/%:0.18~0.20C,0.44~0.62Si,0.85~0.89Mn,0.012~0.015P,0.006~0.009S,0~0.004Ca,0.000 7~0.0010B,0.011~0.088Als)夹杂物钙处理进行了Ca-Al,Al-O,Al-S,Ca-S平衡热力学计算和氧氮分析。得出1 873 KCa]-Al],aO]-Al]和S]-Al]平衡曲线,1 823~1 923 KCa]-S]平衡曲线,和5炉钢对应的实测值。通过分析,得出优化LF精炼工艺:(1)精炼终渣MgO=6%、SiO2<6%、CaO/Al2O3=1.6~1.8;(2)转炉下渣量700 kg左右,精炼终渣量2 000 kg左右;(3)根据精炼终渣CaO/Al2O3=1.6~1.8的目标来决定造渣料的加入量;(4)避免喂钙线时钢水剧烈翻腾,并防止精炼结束到中间包过程钢水的氧化

收稿时间:2015-12-28

Analysis on Slagging Schedule in 100 t LF Refining of Cold Heading Steel SWRCH22A and Process Optimization
Gao Changyi,Zhang Yi,Xie Xiang,Wang Linsong,Zheng Jialiang,Wang Qian.Analysis on Slagging Schedule in 100 t LF Refining of Cold Heading Steel SWRCH22A and Process Optimization[J].Special Steel,2016,37(3):35-38.
Authors:Gao Changyi  Zhang Yi  Xie Xiang  Wang Linsong  Zheng Jialiang  Wang Qian
Affiliation:1 Technology Center; 2 Steelmaking Plant, Shuicheng Iron and Steel Group Corp, Liupanshui 553028; 3 Shuicheng Iron and Steel Group Corp, Liupanshui 553028 ; 4 College of Materials Science and Engineering, Chongqing University, Chongqing 400044
Abstract:In order to reduce inclusions in steel and modify inclusions to prevent nozzle clogging during casting process, the equilibrium theimodynamic calculations of Ca-Al, Al-O, Al-S and Ca-S, and the analysis of oxygen and nitrogen of 5 heats 100 t LF of cold heading steel SWRCH22A (/% : 0.18 ~0. 20C, 0. 44 ~0. 62Si, 0. 85 ~0. 89 Mn, 0.012 ~ 0. 015P, 0. 006 ~ 0. 009S, 0 ~ 0. 004Ca, 0.000 7 -0.001 0B, 0. 011 ~ 0. 088Als) by calcium treatment on inclusions in steel have been carried out. The equilibrium curves of Ca]-Al],aO]-Al] and S] -Al] at 1 873 K and Ca] - S] at 1 823 ~ 1 923 K are obtained and compared to corresponding measured data of 5 heats. By analysis the optimized LF refining process: (1) end refining slag- MgO = 6% , SiO2 <6% and CaO/Al2O3 =1.6 ~1.8; (2) amount of BOF tapping slagging being about 700kg, amount of end refining slag being about 2 000 kg; (3) according to the aim end refining slag with CaO/Al2O3 = 1. 6 ~ 1. 8 to define the amount of charging slag materials; and (4) avoiding the boiling of liquid steel during feeding calcium wire process and the oxidation of liquid during process of end refining to tundish.
Keywords:
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