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    • 61. 发明专利
    • SMELTING AND REDUCING METHOD
    • JPS6328810A
    • 1988-02-06
    • JP16989986
    • 1986-07-21
    • NIPPON KOKAN KK
    • YAMADA KENZOUSUI TSUTOMUIWASAKI KATSUHIROINOUE SHIGERUTANABE HARUYOSHIKAWAKAMI MASAHIROFUKUMI JUNICHI
    • C21B11/00
    • PURPOSE:To remarkably improve the thermal efficiency of a smelting and reducing reaction furnace by blowing up molten slag in the form of liquid drops into the secondary combustion zone in the furnace and causing the secondary combustion of the in-furnace gas at the time of producing a molten iron by using iron ore, reducing agent and auxiliary materials in said furnace. CONSTITUTION:The iron ore, carbonaceous material, slag forming agent, etc., are charged into the reaction furnace 1 of a reverberatory furnace type and gases such as C3H8 and O2 are blown from bottom tuyeres 5 into the furnace. The above- mentioned raw materials are heated and melted by the combustion of the C3H8 and the iron ore is reduced by the carbonaceous material, by which the molten iron 2 and the molten slag 3 are formed. Combustible gases contg. CO, H2, etc., exist as the reactive exhaust gas in the furnace. Gaseous oxygen is blown from an O2 introducing port 6 in the upper part of the furnace to cause the secondary combustion of the combustible gases in the furnace to increase the temp. Powders of CaO, MgO, etc., are blown diagnoally upward with a gas such as O2, N2 as a carrier gas from a nozzle 4 provided at the slag line part into the molten slag 3 and are splashed in the form of liquid drops 7 of the slag into the furnace, by which the temp. thereof is increased and the freshly charged raw materials such as ore are heated. The reaction furnace is thus operated with the good thermal efficiency.
    • 62. 发明专利
    • MELT REDUCTION METHOD
    • JPS62280313A
    • 1987-12-05
    • JP12224686
    • 1986-05-29
    • NIPPON KOKAN KK
    • YAMADA KENZOUSUI TSUTOMUIWASAKI KATSUHIROINOUE SHIGERUTANABE HARUYOSHIKAWAKAMI MASAHIROFUKUMI JUNICHI
    • C21B11/00
    • PURPOSE:To efficiently transmit the heat generated by secondary combustion to a metal bath by burning a carbonaceous material by gaseous O2 so that ore is reduced by melting and splashing the formed metal as splashes to a secondary combustion zone by a gas contg. ore powder. CONSTITUTION:The carbonaceous material and ore are charged into the furnace 1 of the melt reduction furnace. On the other hand, the gaseous O2 is blown from bottom blowing tuyeres 6, etc., into the furnace to burn the above- mentioned carbonaceous material and to reduce the above-mentioned ore by melting, by which the metal bath 2 and slag 3 are formed. The gaseous CO formed by the combustion is secondarily burned by the gaseous O2 blown from tuyeres 4 and the metal bath 2 is heated by the heat generated by the combustion. The gaseous O2 contg. the ore powder is blown from tuyeres 5 to form splashes provided at the position at the height of the metal bath 2 in the above- mentioned operation. The metal of the metal bath 2 is easily splashed as splashes to the secondary combustion zone by the kinetic energy of the ore powder and the gas. The splashes of the metal efficiently absorb the heat generated by the secondary combustion and recover the same in the metal bath 2.
    • 65. 发明专利
    • PRODUCTION OF HIGH-CHROMINUM ALLOY
    • JPS62274019A
    • 1987-11-28
    • JP11489386
    • 1986-05-21
    • NIPPON KOKAN KK
    • USUI TSUTOMUTANABE HARUYOSHIFUKUMI JUNICHIKAWAKAMI MASAHIROYAMADA KENZO
    • C21C7/00
    • PURPOSE:To improve reduction efficiency and to decrease the consumption of a carbonaceous material by blowing Cr ore and the carbonaceous material together gas from side blowing tuyeres into the slag bath in a furnace body of a converter type at the time of specifying an OD ratio and subjecting the Cr ore, etc., to melt reduction in said furnace body. CONSTITUTION:A molten iron 2 is preliminarily put into the furnace body 1, and the Cr ore, charbonaceous material and flux are supplied from a hopper 3 into the furnace body; at the same time, oxygen is blown from a top blowing lance 4 into the furnace body and oxygen is blown from tuyeres 6 for secondary combustion therein to attain iota0.4 OD ratio. Then, the carbonaceous material is subjected to primary combustion by the oxygen from the lance 4 and the gaseous CO generated by such combustion is subjected to the secondary combustion by the oxygen from the tuyeres 6. The slag bath 5 is powerfully stirred when the Cr ore and carbonaceous material are blown together with the oxygen, air or gaseous nitrogen into the slag bath 5 from the side blowing tuyeres 7. A large quantity of heat generated by the primary and secondary combustion is thereby efficiently transferred to the slag bath 5. The reaction contact area of the Cr ore and carbonaceous material in the slag bath 5 is increased and the Cr ore is efficiently reduced.
    • 67. 发明专利
    • METHOD FOR CONTROLLING END POINT OF CONVERTER BLOWING
    • JPS6256513A
    • 1987-03-12
    • JP19530985
    • 1985-09-04
    • NIPPON KOKAN KK
    • KAWAMURA NOBUOFUKUDA MASACHIKATANABE HARUYOSHINAKAMURA HIROMIFUKUMI JUNICHIKAWAKAMI MASAHIRO
    • C21C5/30
    • PURPOSE:To improve the control accuracy of dynamic control by surely executing a sub-lance measurement at the optimum point of the time during blowing. CONSTITUTION:The transition of the concn. of C [C] of a molten steel is estimated by a predicting arithmetic unit 11 from the metallurgical reaction in a converter 1. The decarburization transition point CT at the blowing is determined by an arithmetic unit 13 in accordance with the flow rate Q of a bottom blowing gas in said blowing from the preliminarily obtd. relation between the oxygen blowing rate Q from a bottom blowing device 9 and the decarburization transition point or the preliminarily obtd. transition point in the case of not blowing the gaseous oxygen from the converter bottom. On the other hand, the predicted transition of the concn. of C of the molten steel is inputted to the unit 13 from the unit 11. The unit 13 lowers the sub-lance 6 to sample the molten steel by determining the point of the time when the momentarily decreasing concon. of C of the molten steel attains the decarburization transition point in accordance with such data. The data of the sampling is used for the dynamic control of the end point of blowing, by which the hit rate of the temp. and component compsn. of the molten steel at the end point is increased.
    • 68. 发明专利
    • SLAG COATING METHOD
    • JPS627814A
    • 1987-01-14
    • JP14578385
    • 1985-07-04
    • NIPPON KOKAN KK
    • UCHIDA SHIGETAKATANABE HARUYOSHIFUKUMI JUNICHIKAWAKAMI MASAHIRO
    • C21C5/44
    • PURPOSE:To coat a converter inner wall with slag in a short time after tapping, by tapping molten steel after a steel making refining by the converter, throwing a reducing agent to a residual molten slag to lower its temp. by endothermic reaction in reduction of iron oxide in the molten slag and increasing the viscosity. CONSTITUTION:The refined molten steel in converter operation is tapped, and the excess molten slag is discharged while leaving a prescribed quantity of molten slag in the furnace. About 1/3 of quick lime, dolomite, etc. being flux to be used in next time charging is thrown to the remaining slag, and a suitable quantity of cokes being the reducing agent is added. After lowering the temp. of molten slag and increasing its viscosity by the reduction endothermic reaction of iron oxide in the molten slag due to the addition of flux being cooling material and cokes, the converter is turned and moved slightly. Thereby, the slag for protecting inner wall of the converter is coated in a short time after tapping.