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    • 4. 发明专利
    • METHOD FOR CHARGING RAW MATERIAL INTO BLAST FURNACE
    • JPH01208409A
    • 1989-08-22
    • JP3466288
    • 1988-02-16
    • KOBE STEEL LTD
    • MIYATANI HITOSHIFUNABIKI TETSUSHIYUZUKUBO YASUMASA
    • C21B5/00
    • PURPOSE:To stably keep center flow operation by controlling the specific raw material charging pressure from charging chute at axial center part in accordance with raw material piling level in a furnace and adjusting reached position of the specific raw material. CONSTITUTION:After storing the specific raw material separating to a chute 10 from a charging conveyor 6 to a storing vessel 11, it is charged into a hopper 14 through a slide gate 12, discharging feeder 13. After storing this in a pressurizing chamber 19, it is charged into the axial center part from a charging chute 9. Coke-ore alternative piling state in the furnace is measured with a measuring instrument 2 and profile meter, and based on the result, a working valve 17 or discharging pressure valve 18 in N2 supplying line l1 and N2 discharging line l2 are opened/closed to increase/decrease the pressure in the pressurizing chamber 19. By this method, the discharging speed of the specific raw material discharged from the charging chute 9 is adjusted to stably execute blast furnace operation under good productivity.
    • 7. 发明专利
    • METHOD FOR REFINING MOLTEN IRON
    • JPS648210A
    • 1989-01-12
    • JP16418887
    • 1987-07-01
    • KOBE STEEL LTD
    • MIYATANI HITOSHINISHIHARA TAKASHIFUJIWARA HIROSHI
    • C21C1/00C21C1/02C21C1/04
    • PURPOSE:To uniformly disperse refining agent in molten iron and to improve efficiency of refining reaction by arranging auxiliary nozzle hole for blowing gas at upper part of nozzle hole of an injection lance blowing the powdery refining agent in the molten iron. CONSTITUTION:The injection lance 5 is almost vertically inserted into the molten iron 2 in desiliconizing refractory 1. The desiliconizing agent flowing passage 4 is formed at the axial position of this lance 5 and connected with the refining agent blowing nozzle 10. Further, plural auxiliary gas flowing passages 7 are formed around the desiliconizing agent flowing passage 4 to connect respectively to the auxiliary nozzle holes 11, and the auxiliary nozzle hole 11 is positioned at upper part of opening position of refining agent blowing nozzle. By this constitution, at the time of blowing the desiliconizing agent 8 carrying from a tank 9 with carrier gas G into the molten iron 2 from the blowing nozzle 10, the carrier gas G becomes relatively large bubble and floated up. At this time, the auxiliary gas Ga is injected as jet flow from the auxiliary nozzle 11 through the auxiliary flowing passage 7 and the floated bubble is subdivided to make fine bubbles and the contacting area between the desiliconizing agent 8 and the molten iron 2 is increased.
    • 8. 发明专利
    • METHOD FOR OPERATING ELECTRIC REFINING FURNACE
    • JPH09137211A
    • 1997-05-27
    • JP29013995
    • 1995-11-08
    • KOBE STEEL LTD
    • ARIZUKA MITSUHIROMIYATANI HITOSHITAKEUCHI SHINJIROKIGUCHI JUNPEI
    • C21B11/10F27B3/08F27B3/20
    • PROBLEM TO BE SOLVED: To improve productivity and to stabilize operation by increasing the charging ratio of a reducing agent on a furnace core side and lowering the rate on the peripheral side of the furnace in operation of the electric refining furnace to be charged with ore and the reducing agent. SOLUTION: Raw materials of a low cake ratio (coke/ore) are charged into a raw material tank for charging to the peripheral part of the furnace among the raw material tanks disposed in the upper part, and the raw materials of the high coke ratio are charged into the raw material tank for charging to the core part of the furnace in the operation of the electric refining furnace to execute reduction by charging the ore and the reducing agent (usually coke) into the furnace and melting the raw materials by electric energy. If the respective raw materials are charged dividedly into the furnace in this constitution, the electric resistance value in the furnace increases and the gas (CO) generated in the furnace is effectively utilized for the indirect reduction of the core in the upper part. As a result, the production efficiency is improved and the operation is stabilized.