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    • 71. 发明专利
    • SMELTING, REDUCING AND REFINING EQUIPMENT
    • JPS6347308A
    • 1988-02-29
    • JP19246286
    • 1986-08-18
    • NIPPON KOKAN KK
    • FUJII SHIRO
    • C21B13/00C21B13/14
    • PURPOSE:To stabilize the operation of a smelting and reducing furnace and to produce a molten iron at a low cost by adequately controlling the temp. and degree of oxidation of the exhaust gas of a reducing furnace at the time of producing the molten iron by charging iron ore, coal, lime, etc., into the smelting and reducing furnace and blowing gaseous oxygen to the furnace. CONSTITUTION:The molten iron is produced by blowing the iron ore preheated and prereduced in a prereducing furnace 3 as well as the powder of the coal and lime into the molten iron in the smelting and reducing furnace 1 and blowing O2 to the furnace from a lance to reduce the iron ore with the C of the coal. The exhaust gas 2 emitted from the reducing furnace 1 at this time is as extremely high as 1,500-1,800 deg.C; therefore, the exhaust gas from the prereducing furnace 3 is subjected to recovery of sensible heat by a dust collector 4 and a heat recovery device 5, then to sepn. of CO2 in a CO2 recovery device 6. The remaining Co- and H2-contg. gas is supplied to the down stream stage. The CO2 is partly liquefied in a liquefying device 8 and the balance is mixed with the high-temp. exhaust gas from the smelting and reducing furnace 1 by a blower 7 to control the temp. thereof to 1,150-1,250 deg.C most adequate for the prereduction of the iron ore. The degree of oxidation is also adjusted to an adequate value and such gas is supplied to the prereducing furnace 3, by which the prereducibility is controlled to a specified value and the fluctuation in the operation of the smelting and reducing 1 is prevented.
    • 72. 发明专利
    • SMELT-REDUCTION REFINING EQUIPMENT
    • JPS6342317A
    • 1988-02-23
    • JP18457586
    • 1986-08-06
    • NIPPON KOKAN KK
    • FUJII SHIRO
    • C21B13/00C21B13/14
    • PURPOSE:To enable the direct production of oxygen gas by utilizing energy in exhaust gas, by heating steam from a steam turbine by introducing the exhaust gas from a smelting reduction furnace to a heat exchanger and connecting a deoxygenating apparatus with an air compressor driven by this steam. CONSTITUTION:After using the high temp. exhaust gas from the smelting reduction furnace 1 to pre-reduction 2, the gas is supplied to the heat exchanger 4 through a dust collector 3. The heat exchanger 4 is connected with the steam turbine 5 by piping 20 and after heating the circulated steam by the heat exchanger 4, it is supplied to the steam turbine 5, to drive the steam turbine 5 and the air compressor 7. The compressor 7 supplies the compressed air to the deoxygenating apparatus 8. The deoxygenating apparatus 8 separates the oxygen gas from the compressed air, to supply the oxygen to the smelting reduction furnace 1. In this way, the power consumption for producing oxygen gas is reduced.
    • 75. 发明专利
    • PRODUCTION OF REDUCED IRON
    • JPS62238310A
    • 1987-10-19
    • JP7983386
    • 1986-04-07
    • KAWASAKI HEAVY IND LTD
    • SUZUKI MASANORIMITSUTA SUSUMU
    • C21B13/00C21B13/14
    • PURPOSE:To decrease the quantity of the heat to be supplied from the outside of the system and to reduce cost by withdrawing part of a fluid medium from the 2nd reduction furnace to reduce preliminarily reduced iron to metallic iron, separating carbonated lime therefrom and charging the same into the 1st reduction furnace. CONSTITUTION:The preliminarily reduced iron from the 1st reduction furnace as well as reducing gas and CaO are charged into the 2nd reduction furnace 2. Part of the fluid medium is withdrawn from the furnace and is magnetically separated to reduced iron and carbonated lime by a separator 5. The carbonated lime is charged together with iron ore, 2nd reduction furnace exhaust gas and oxygen into the 1st reduction furnace 1, by which the preliminary reduction of the iron ore, the regeneration of CaO of the carbonated lime and the replenishment of CaO by the supply of limestone are executed. The preliminarily reduced iron formed in such a manner is charged into the 2nd reduction furnace 2. The rate of utilization of the reducing gas is improved and the sulfur-component in the preliminarily reduced iron is decreased by the above-mentioned method.