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    • 2. 发明专利
    • METHOD FOR MELTING LOW MANGANESE STEEL
    • JPH1161221A
    • 1999-03-05
    • JP24187497
    • 1997-08-22
    • KAWASAKI STEEL CO
    • OSHIMA KENJIOKUDA HARUYUKIEBARA TAKESHI
    • C21C5/28C21C5/32C21C5/36C21C7/00
    • PROBLEM TO BE SOLVED: To efficiently lower Mn without accompanying extremely lowering Cf in a converter operational process and to secure the quality of an electric steel sheet, etc., without bringing about the rising of N in the steel by specifying the basicity and the total Fe content in converter slag. SOLUTION: The slag basicity (the ratio of SiO2 to the total CaO charged into the converter) is adjusted to 3.0-4.0 to achieve low Mn while restraining such FeO content in the slag as to keep the finish carbon Cf at the time of blowing off. Further, the total Fe content in the converter slag is restrained to in the range of 15-25%. At the time of executing the converter operation so as to satisfy the above condition, the low Mn steel can be produced while keeping the Cf to almost 0.035%, but MgO content in the slag may be adjusted to 8-11% in order to further rise the Mn partition ratio. After completing the check of the steel components and the measurement of the temp. etc., wish a sub-lance at the end stage of the converter operation, the suitable quantity of slag-making material of iron ore, SiO2 , Cab, etc., is added to adjust the slag composition.
    • 7. 发明专利
    • PROTECTING METHOD FOR DOUBLE PIPE TUYERE
    • JPS6274017A
    • 1987-04-04
    • JP21304085
    • 1985-09-26
    • KAWASAKI STEEL CO
    • OKUDA HARUYUKITAKE HIDEO
    • C21C5/34C21C5/48
    • PURPOSE:To prevent the wear of the double-pipe tuyere provided to the side part or bottom part of a refining furnace such as converter by specifying the timings for opening and closing selector valves for a refining gas, cooling gas and inert gas to the inside and outside pipes of the tuyere. CONSTITUTION:The double-pipe tuyere is constituted of the outside pipe 1 and the inside pipe 2. The refining gas is blown into the converter from the pipe 2 and the cooling gas from the pipe 1 (state A). The inert gas is blown from the pipes 2, 1 when the converter 7 tilts and while the tuyere 8 is not is contact with a molten metal (state B). The state B is the state in which valves 12, 14 are open. The timings for opening and closing the selector valves are controlled in accordance with the volume and flow rate of the gas in the piping from the selector valves of the inside and outside pipe lines 10, 9 up to the tuyere 8 in the stage of changing the state B to the state A. The blowing of the cooling gas is started at >=1sec before start of blowing in the state of starting the blowing of the refining gas. The blowing of the cooling gas is stopped with >=1sec delay than at the end of blowing in the stage of ending the blowing of the refining gas.