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    • 21. 发明专利
    • PREHEATING AND REDUCING DEVICE FOR IRON ORE
    • JPS62227022A
    • 1987-10-06
    • JP7157686
    • 1986-03-28
    • NIPPON STEEL CORP
    • HAYASHI YOICHINISHIHARA NOBUYOSHIEGASHIRA TATSUHIKONAKAMURA MASAKAZUKATAYAMA TSUTOMU
    • F27B15/00C21B13/00C21B13/14
    • PURPOSE:To efficiently preheat and reduce a granular raw material without splashing to the outside of the system by combining a suspension preheater, fluidized bed preheating furnace, fluidized bed preliminary reduction furnace and out-of-furnace circulation system to constitute a preheating and reducing device for powdery iron ore. CONSTITUTION:The powdery iron ore 1 and limestone 2 are preheated by the suspension preheater consisting of a high-temp. exhaust gas flue 24, a piping 25 and a multi-stage cyclone 26 of the fluidized bed preheating furnace 3. The coarse grains directly enter the preheating furnace 3 and the pulverized powder is recovered in the cyclone 26 via a piping 25 by the exhaust gas and flows into the preheating furnace 3. Coal 7 and air 5 from the furnace bottom are blown into the preheating furnace 3 to burn the above-mentioned raw material, by which the raw material is heated and decarbonized. The quicklime formed in such a manner is introduced into the fluidized bed preliminary reduction furnace 6 where the iron ore is preliminarily reduced by the reducing exhaust gas from the melt reduction furnace 10. The pulverized powder is recovered and preliminarily reduced by the outside circulation system 33 including the cyclone 34. The powder is heated by a pulverized coal burner 39 in the final fluidized bed preliminary reduction furnace 6. The coarse grained raw material 41 and pulverized powder raw material 40 are supplied by respective feeders to the melt reduction furnace 10. The iron ore and other raw materials are preliminarily reduced and heated at a good raw material yield and thermal efficiency.
    • 22. 发明专利
    • TREATMENT OF COKE POWDER IN DRY COKE QUENCHING INSTALLATION
    • JPS61145286A
    • 1986-07-02
    • JP26725884
    • 1984-12-18
    • NIPPON STEEL CORP
    • EGASHIRA TATSUHIKONISHIHARA NOBUYOSHI
    • C10B39/02
    • PURPOSE:To collect a combustible material in a high-temp. circulation gas after cooling coke, to recover heat by burning it in a two-stage fluid layer furnace, to mix a part of a hot gas with the high-temp. circulation gas and to subject a part of a cold gas from a heat exchanger to effectuation treatment such as temp. control for the fluid layer. CONSTITUTION:A dry coke equenching installation is so constituted that high- temp. coke is cooled in a circulation gas and a combustible material is removed from the circulation gas by a dust collector 2, 12 after cooling coke, and sensible heat is recovered by a heat exchanger 16, 22. The combustible material collected by the dust collector is burned in a fluid layer furnace 6 constituted of a fluid layer combustion zone and a combustion zone thereabove provided with a sub heat exchanger 22 in the free board. A part of the combustion heat is recovered by the sub-heat exchanger 22 and a hot gas evolved from the furnace 6 is mixed with the high-temp. circulation gas prior to entering the heat exchanger 16. A part of a cold circulation gas coming out of the heat exchanger 16 is blown into the furnace 6 to control the temp. of the fluid layer.
    • 30. 发明专利
    • PRETREATMENT OF COAL AND FACILITY THEREFOR
    • JP2000290665A
    • 2000-10-17
    • JP9824299
    • 1999-04-05
    • NIPPON STEEL CORP
    • EGASHIRA TATSUHIKO
    • C10B47/00C10B57/02C10B57/08C10B57/10
    • PROBLEM TO BE SOLVED: To provide a coal-treating method for production of coke, capable of preventing concentration of tar content and coal powder in circulation gas of a quick heating process, lowering the acidic gas concentration impairing the quality of heated coal and carrying out a heat treatment in a reducing gas atmosphere and facility therefor. SOLUTION: Hot air generated in a hot air generating furnace 2 is blown into a drying classifier 1 to dry coal and the dried crude particles and fine powder are rapidly heated in stream heating towers 8-1 and 8-2 to pyrolyze the crude particles and fine powder and the resultant gas is separated by solid- gas separators 9-1 and 9-2 and the separated gas is circulated through a circulation line 10 into a stream heating tower to carry out a drying treatment of coal for production of coke. A fuel gas is blown from a fuel gas-blowing line 11 into a circulation gas of the circulation line 10 and a part thereof is circulated into the stream heating towers 8-1 and 8-2 and a part thereof is fed to a burner 13 for hot air-generating furnace 2 by a gas feed line 12.