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    • 2. 发明专利
    • METHOD FOR REFINING MOLTEN STEEL
    • JPH0925507A
    • 1997-01-28
    • JP17352695
    • 1995-07-10
    • NIPPON KOKAN KK
    • KAMEMIZU AKIRAFURUNO YOSHIKATSUFUKUMI JUNICHITOYODA KOJI
    • C21C7/00C21C7/04C21C7/06C21C7/068C21C7/10
    • PROBLEM TO BE SOLVED: To efficiently produce a high clean aluminum killed extra-low carbon steel by adding CaO during tapping molten steel roughly decarburized steel to lower the m.p. of slag, further executing an Al deoxidation after executing a vacuum decarburization and successively, executing a stirring refining. SOLUTION: The molten steel roughly decarburized steel in a refining furnace is tapped into a ladle and the molten steel in this ladle is vacuum-decarburized and refined in RH degassing equipment. At this time, CaO is added during tapping to lower the m.p. of slag and successively, the Al deoxidation is executed after vacuum deoxidizing in the condition of undeoxidation. The composition of ladle slag during modifying and after modifying the slag is desirable to be made into 5±0.2 basicity CaO/SiO2 and 1.5±0.1 CaO/Al2 O3 by charging the CaO. Thereafter, the molten steel is sufficiently stirred with the slag in simple refining equipment capable of the gas stirring and an alloy addition, and refined. By this method, the adjustment of components in the molten steel is executed, and also iron oxide in the slag is reduced to execute the slag modification.
    • 8. 发明专利
    • OXYGEN NOZZLE FOR SECONDARY COMBUSTION OF CONVERTER
    • JPH01252721A
    • 1989-10-09
    • JP8048788
    • 1988-03-31
    • NIPPON KOKAN KK
    • MURAKI YASUNORIHASEGAWA TERUYUKITOYODA KOJI
    • C21C5/46
    • PURPOSE:To perfectly carry out the secondary combustion of the CO-contg. gas in a converter and to improve the heat efficiency by inserting a nozzle tip having many small holes into the secondary-combustion oxygen nozzle at the tip of a lance at the time of decarburizing and refining molten iron in the converter having a top-blowing oxygen lance to produce molten steel. CONSTITUTION:The moten iron, which has been desulfurized, dephosphorized, etc., is charged into an top-blown converter, oxygen is blown into the converter from the oxygen nozzle 11 of an oxygen top-blowing lance 10 to oxidize the C in the molten iron, and then molten iron is decarburized to produce molten steel. In this case, the gaseous CO generated by the oxidation of C in the molten iron is secondarily burned to improve heat efficiency. For the purpose, the nozzle tip 1 obtained by embedding small pipes 3 made of heat-resistant metal into a refractory material 4 is inserted into the secondary-combustion oxygen nozzle 12 opened obliquely downward at the tip of the lance 10. Gaseous O2 for the secondary combustion of CO is rapidly diffused into a CO-contg. atmosphere, CO is secondarily burned with high efficiency, and the heat efficiency of the steelmaking oxygen top-blown converter is remarkably improved.
    • 9. 发明专利
    • METHOD FOR CONTROLLING CARBON CONTENT AT END POINT IN CONVERTER
    • JPH01247526A
    • 1989-10-03
    • JP7475188
    • 1988-03-30
    • NIPPON KOKAN KK
    • YAMADA KAORUMIYAHARA HIROAKITOYODA KOJIISHIKAWA HIROAKI
    • C21C5/30
    • PURPOSE:To control the aimed carbon content in molten steel at end point in a converter at good accuracy by refining dephosphorized molten iron in the converter, measuring the carbon content and temp. in the molten steel at end stage of blowing and finding the necessary blowing oxygen rate with the specific decarbonizing equation. CONSTITUTION:At the time of refining the dephosphorized molten iron with less-slag in the converter, the carbon content and temp. in the molten steel in the converter are measured at the end stage of the blowing. By using these measured values, the decarbonizing model (in the equation, C: carbon content in the molten steel, Q: blowing oxygen rate, CT: transition point of decarbonization, CL: limiting point of decarbonization, alpha, beta: the content) is integrated with relation between the present carbon content and the aimed carbon content, and the necessary blowing oxygen rage is found to execute the blowing. Further, the decarbonizing transition point of this corresponding heat is calculated from the actual blowing data and feed-back thereof is executed to the next heat as the decarbonizing transition point CT. By this method, the carbon content and temp. at the end point in the converter is controlled at high accuracy.