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    • 34. 发明专利
    • Controlling method for finish temperature of converter operation
    • 转炉运行完成温度控制方法
    • JPS5770215A
    • 1982-04-30
    • JP14436480
    • 1980-10-17
    • Nippon Kokan Kk
    • TERADA OSAMUHASEGAWA TERUYUKIYAMASE OSAMUEDANE TOSHIO
    • C21C5/30C21C5/32
    • C21C5/32Y02P10/212
    • PURPOSE:To improve the adequteness degree of the finish temperature of a converter operation and control the finish temperature at the optimum value by a method wherein a correction term determined by the mixing ratios of molten pig iron is added to a temperature rise model used for a dynamic control of the finish temperature of a converter operation for refining. CONSTITUTION:For the dynamic control of the finish temperature of the converter operation for refining, a temperature rise model is used which represents the temperature rise rate per unit amount of blown oxygen dT/dQ in terms of the factors as follows: dT/dQ=F([C]i, Bi, Fi, Ei, Oi, Ii, Ki,). where i is the heat number, [C] is the carbon content of the steel bath, Q is the amount (Nm ) of blown oxygen, B is the blowing pattern, F is the amount of flux charged, E is the contents of other components (Si, Mn, P, etc.), O is the amount of iron ores charged, I is the initial conditions and K is a model factor. To this basis temperature rise model is added the correction term which depends on the amount of undissolved scraps and is determined by the mixing ratios of the molten pig iron. Accordingly, it is made possible to control the finish temperature following up to the change in the mixing ratios of the molten pig iron.
    • 目的:提高转炉运行终点温度的正确度,并通过一种方法将最终温度控制在最佳值,其中将通过熔融生铁混合比确定的修正项加到用于 用于精炼的转炉操作的终止温度的动态控制。 构成:为了精炼转炉运行的终止温度的动态控制,使用温升模型,其代表根据以下因素的每单位吹氧量DT / dQ的升温速率:dT / dQ = F([C] i,Bi,Fi,Ei,Oi,Ii,Ki)。 其中i是热数,[C]是钢浴的碳含量,Q是吹氧的量(Nm 3),B是吹塑图案,F是充入的量的量,E是 其他组分(Si,Mn,P等)的含量,O是铁矿石的含量,I是初始条件,K是模型因子。 在此基础上,增加温升模型,该校正项取决于未溶解废料的量,并由熔融生铁的混合比决定。 因此,随着熔融生铁的混合比的变化,能够控制最终温度。
    • 36. 发明专利
    • Steel-making process by converter
    • 转炉制钢工艺
    • JPS5739113A
    • 1982-03-04
    • JP11346880
    • 1980-08-20
    • Nippon Kokan Kk
    • OZEKI AKIYAHASEGAWA TERUYUKINIMURA YOUICHIYAMADA KENZOUUSUI TSUTOMUTAMURA KOUNOSHINEDANE TOSHIO
    • C21C5/34C21C5/32C21C5/35C21C5/48
    • C21C5/35
    • PURPOSE:To reduce the unit product of an agitating gas and also to prevent the fusion and damage and the clogging of a tuye re, by flowing from bottom of an inert gas or CO2 gas diluted by O2 gas as an agitating gas together with blowing of O2 from top. CONSTITUTION:White O2 gas is blown into molten steel 3 from a lance 2 for blowing from top, an inert gas or CO2 gas from a CO2 gas source 7 diluted by O2 gas from an O2 gas source 8 is blown as an agitating gas into the molten steel 3 from the tuye re 4 under the surface of molten steel 3 in the furnace. The suitable inert gas is Ar gas and the inert gas and CO2 gas may be used in combination. Further, the total amount of a gas blown from bottom is about 1/3-1/3,000 of that of O2 gas blown from top.
    • 目的:为了减少搅拌气体的单位产物,并且通过从作为搅拌气体的O 2气体稀释的惰性气体或二氧化碳气体的底部流出,同时防止熔融,损坏和堵塞,同时吹入 O2从顶部。 构成:将白色的O 2气体从用于从顶部吹出的喷枪2吹入钢水3中,将来自O 2气体源8的由O 2气体稀释的CO 2气体源7的惰性气体或二氧化碳气体作为搅拌气体吹入 钢水3从钢管3中的钢管3在炉内。 合适的惰性气体是Ar气体,惰性气体和二氧化碳气体可以组合使用。 此外,从底部吹出的气体的总量为从顶部吹出的O 2气的总量的大约1 / 3-1 / 3,000。