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    • 101. 发明专利
    • SMELTING REDUCTION IRON-MAKING METHOD
    • JPH02209409A
    • 1990-08-20
    • JP2855489
    • 1989-02-09
    • NIPPON KOKAN KK
    • KITANO YOSHIYUKIARAKAWA SAKAETSUBOI HARUTOISOZAKI SHINICHIIWASAKI TOSHIHIKO
    • C21B11/00C21B13/00
    • PURPOSE:To efficiently execute smelting reduction iron-making provided with a pre- reduction furnace by alternately executing slag tapping and iron tapping in plural smelting reduction furnaces, continuously operating the smelting reduction and preventing lowering of supplying gas into a pre-reduction furnace. CONSTITUTION:Generating gas of the smelting reduction furnace 2A is supplied into the pre-reduction furnace 1. The pre-reduction is executed to powdery ore charged in this pre-reduction furnace 1 as fluidized bed 5 with the above generated gas. In the obtd. pre-reduction ore, the coarse grain is charged through an ore discharging tube 6 and the fine grain is charged through a dust collector 4 with carrier gas, into the smelting reduction furnace 2A, respectively, and the smelting reduction is executed to obtain molten iron. In the above pre-reduction-smelting reduction iron-making method, to one set of the pre-reduction furnace 1, two or more sets of smelting reduction furnaces 2A, 2B for supplying the generating gas into the above furnace 1, are arranged. The slag tapping and iron tapping are alternately executed from the furnaces 2A, 2B so as to execute the continuous operation of the smelting reduction. By this method, the continuous supply of the raw material from the pre-reduction furnace 1 can be executed, and the miniaturization thereof can be realized and fluidization of the fluidized bed 5 can be maintained under good condition.
    • 103. 发明专利
    • SMELTING REDUCTION IRON-MAKING EQUIPMENT
    • JPH02175808A
    • 1990-07-09
    • JP32936188
    • 1988-12-28
    • NIPPON KOKAN KK
    • ARIYAMA TATSUROISOZAKI SHINICHI
    • C21B11/00C21B13/00
    • PURPOSE:To effectively utilize excess energy in the system and to reduce unit consumption of coal by using a parallel flow type rotary drying machine to prevent over-heat, etc., of the coal developing in the case of using a counter flow type and executing suitable drying and preheating without developing sintering, etc. CONSTITUTION:This smelting reduction iron-making equipment is formed with a smelting reduction furnace 1, fluidized bed type pre-reduction furnace 2, to which the gas generated in the furnace 1 is supplied, the parallel flow type rotary drying machine 3, a system 4 for supplying the coal to the drying machine, waste gas supplying system 5 and a system 6 for supplying dried and preheated coal discharged from the above drying machine 3 into the above smelting reduction furnace 1. The above drying machine 3 drys and preheats the coal 4 as the carbonaceous material. Further, in the above waste gas supplying system 5, after removing dust in the waste gas generated from the pre- reduction furnace 2, this is supplied to the drying machine 3.
    • 104. 发明专利
    • METHOD AND DEVICE FOR PRODUCING POLYCRYSTALLINE SILICON
    • JPH0230611A
    • 1990-02-01
    • JP18020188
    • 1988-07-21
    • NIPPON KOKAN KK
    • ARIYAMA TATSUROISOZAKI SHINICHI
    • C01B33/03
    • PURPOSE:To prevent the deposition of silicon on the inside surface of a reactor by supplying and decomposing a silicon-containing gas under conditions that silicon particles are heated and circulated with flowing in the reactor. CONSTITUTION:An inner cylinder 4, a ling 6 having a diameter smaller than the inner cylinder 4 (on a bottom plate 3), a dispersing plate 7 and a circular gas nozzle 8 for driving the particles are disposed in a reactor 2. Mixed gases of a silicon-containing gas and hydrogen gas are introduced into the inner cylinder 4 through the dispersing plate 7 to fluidize silicon particles in the inner cylinder 4 and the silicon particles raised together with the gases are heated from the outside of the reactor 2 with a heat-supplying device 15 while being sunk in the circular portion 14 of a double cylinder. The sunk heated silicon particles are moved and fluidized in the cylinder with a gas 11 sent by a driving gas nozzle 8 disposed in the bottom plate 3 in a circular state. Heat is supplied to the fluidized layer with the sensible heat of the silicon particles and the silicon particles are brought into contact with the send silicon-containing gas 10 to subject the silicon-containing gas to a pyrolysis or reduction reaction, thereby allowing the silicon to deposit and grow on the surfaces of the silicon particles.