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    • 4. 发明专利
    • METHOD FOR ESTIMATING DISTRIBUTION OF CARBON CONCENTRATION IN HEIGHT DIRECTION OF SINTERED LAYER
    • JPH03240926A
    • 1991-10-28
    • JP3570690
    • 1990-02-16
    • NIPPON KOKAN KK
    • NAKAJIMA RYUICHIKISHIMOTO SUMIYUKIKUROSAWA SHINICHIMATSUNAGA YOSHIFUMIFUKUYO HIROSHIWADA TAKASHI
    • C22B1/20
    • PURPOSE:To exactly detect the distribution of the carbon concn. in the height direction of a sintered layer in a short period of time by inputting the respective measurement signals of the carbon concn. measuring instruments, gas flow meters and gas thermometers mounted to respective window boxes to a computing machine and making prescribed computations. CONSTITUTION:The measurement signals of the respective flow meters mounted to the respective window boxes(WB) of a DL type sintering machine are sent to a computing section 22 for the distribution of the gas flow rate in the longitudinal direction of the computing machine 20. The measurement signals necessary for determining the position and thickness of the rod hot layer in the longitudinal direction of the machine of the respective gas thermometers, etc., are sent to a computing section 21 for the position and thickness of the red hot layer in the longitudinal direction of the machine. The measurement signals of the respective CO and CO2 concn. measuring instruments and the results (signals) of the computations of a computing section 22 are sent to a computing section 23 which computes the distribution of the carbon concn. in the respective positions in the longitudinal direction of the machine by prescribed equation. The results (signals) of computation of the section 23 are sent together with the results of computation of the section 21 to a computing section 24 where the carbon concn. in the height direction of the sintered layer is computed by prescribed equation. The results of the computation are displayed on a CRT display 25. The distribution of the carbon concn. in the height direction of the sintered layer is controlled in real time in this way.
    • 6. 发明专利
    • OPERATION OF BLAST FURNACE
    • JPH03215612A
    • 1991-09-20
    • JP1088290
    • 1990-01-19
    • NIPPON KOKAN KK
    • NAKAJIMA RYUICHIKISHIMOTO SUMIYUKIHOTTA HIROHISA
    • C21B5/00
    • PURPOSE:To blow pulverized coal and flux into a furnace in uniformly mixing condition by laying the flux at the specific ratio on unpulverizing coal on a conveyor and pulverizing after charging and mixing them into a mixer at the time of producing mixed material of the pulverized coal and flux for blowing from a tuyere in the blast furnace. CONSTITUTION:In the case of reducing Si content in molten iron tapping from the blast furnace by blowing the mixed material of the pulverized coal and flux powder from the tuyere in the blast furnace, the unpulverizing coal 2 is laid on the belt conveyor 3, and the flux 4 is laid thereon at the quantity so as to become 2-10wt.% of the total quantity of coal 2 and flux 4 and mixed in the mixer 1, and after stirring they are pulverized. The mixing ratio of both in the pulverized mixture is prevented a variance and the mixture become the mixed fine powder having uniform composition, and by blowing them into the blast furnace from the tuyere, the Si content in the molten iron in the furnace is effectively reduced.
    • 7. 发明专利
    • OPERATION OF BLAST FURNACE
    • JPH03215611A
    • 1991-09-20
    • JP1088190
    • 1990-01-19
    • NIPPON KOKAN KK
    • NAKAJIMA RYUICHIKISHIMOTO SUMIYUKIHOTTA HIROHISA
    • C21B5/00
    • PURPOSE:To effectively reduce Si in molten iron by supplying pulverized coal and flux into a tuyere from outlet of a storing vessel in alternately laminating condition in the same storing vessel at the specific ratio at the time of reducing the Si content in the molten iron by blowing the mixed power of the pulverized coal and the flux from the tuyere in the blast furnace. CONSTITUTION:At the time of reducing the Si content in the molten iron in the furnace by blowing the pulverized coal and flux powder from the tuyere in the blast furnace, the fixed quantity Q of pulverized coal 2 is supplied into the storing vessel 1 during the fixed time T1, and after stoppage time T2, again the pulverized coal 2 is supplied. The fixed quantity of flux powder 3 is supplied in the storing vessel 1 as the showed pattern 2 during the above mentioned pulverized coal supply stoppage time T2, and the pulverized coal layer and the flux layer are alternately laminated. In this case, the quantity per one layer for each pulverized coal and flux, is made to =100. By discharging the pulverized coal and the flux from the outlet 4 in the storing vessel 1 under this condition, both raw materials are uniformly mixed and blown in the furnace, and Si content in the molten iron in the furnace is effectively reduced.
    • 8. 发明专利
    • METHOD FOR UNIFORMLY MIXING COALS FOR PULVERIZED COAL
    • JPH03213131A
    • 1991-09-18
    • JP905090
    • 1990-01-18
    • NIPPON KOKAN KK
    • NAKAJIMA RYUICHIKISHIMOTO SUMIYUKIIINO BUNGOITO HARUOFURUYA SHIGEKI
    • B01F3/18
    • PURPOSE:To stably mix coals by delivering different coal components in a predetermined mixing ratio by a quantitative delivery apparatus and stacking the same on the previously delivered coal on a conveyor scale to mix the coals by a mixer to ground the same by a grinder: CONSTITUTION:A follow transport apparatus 4 equipped with the quantitative delivery apparatus 4a connectable to a follow coal storage tank 2 storing coal whose components are different from those of the coal in a main coal storage tank 1 is allowed to make connection with a main feed apparatus 3 equipped with the conveyor scale 3a connectable to the main coal storage tank 1. A coal mixer 5 and a feed apparatus 6 reaching a coal grinder from the mixer 5 are arranged to one end of the apparatus 3. Coal is charged in the apparatus 3 in an indicated mixing ratio from the tank 1 and other coal is charged in the apparatus 4 in an indicated mixing ratio from the tank 2 to be stacked on the previously charged coal from the connection part to the apparatus 3 and both coals are charged in the mixer 5 from one end of the apparatus 3 to be mixed each other while the coal mixture is charged in the coal grinder by the apparatus 6 to be ground.