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机构地区:[1]江苏省(沙钢)钢铁研究院,江苏张家港215625
出 处:《炼钢》2016年第2期12-17,共6页Steelmaking
摘 要:针对铝镇静无取向硅钢冶炼过程中钢水、炉渣氧势过高,导致RH终点钢水总氧含量控制不稳定的问题,进行了转炉出钢、RH过程脱氧造渣工艺优化研究。结果表明:RH进站钢水砌(O)由原工艺的(400-900)×10^-6稳定在650×10^-6以下,RH脱碳结束钢水w(O)控制在450×10^-6以下;RH进站炉渣w(T.Fe)由原工艺的10%~25%降至15%以下,RH出站渣中w(T.Fe)由2%~12%降至3%以下,RH处理过程炉渣碱度均控制在3.0以上;RH终点侧(T.O)由原工艺的(15~30)×10^-6降至15×10^-6以下,钢水洁净度较原工艺显著改善。To the question of the unsteadiness of the steel oxygen content at the end of RH vacuum treatment for the aluminium deoxidization non-oriented silicon steel refining, the oxygen potential of molten steel and slag was optimized during tapping and deoxidation alloying process. Results show that the oxygen mass fraction of non-oriented silicon steel is stably controlled below 650 ×10^-6 as it was (400 - 900) ×10^-6 before optimization. Furthermore, T. O mass fraction is controlled below 450 ×10^-6 at the end of decarbenization in RH. With the optimization process, the mass fraction of T. Fe in slag is decreased from 10 % - 25 % to less than 15 % at the beginning of RH, which is also decreased from 2 % - 12 % to below 3 % at the end of RH, and the slag basicity is controlled above 3.0 during RH treatment process. T. O mass fraction at the end of RH is reduced from (15 - 30) ×10^-6 to below 15 ×10^-6 using the optimization process, which indicated that the cleanliness of molten is significantly improved.
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