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    • 45. 发明专利
    • PROCESS SYSTEM CONTROLLING METHOD
    • JPH11259144A
    • 1999-09-24
    • JP6312298
    • 1998-03-13
    • TOSHIBA CORP
    • IINO MINORU
    • G05B13/04C04B7/36C04B7/38G05D11/13
    • PROBLEM TO BE SOLVED: To maintain product quality and to attain the optimum utilization of a system in economical and environmental viewpoints. SOLUTION: The method is provided with a 1st step 2 for estimating the states of plural raw materials based on the blending ratio of the plural raw materials supplied to a 1st process 120 for manufacturing intermediate products by mixing plural raw materials and on the states of the intermediate products, a 2nd step 4 for estimating a quantity of heat necessary for heat-treatment in a 2nd process 140 for heating the intermediate products, a 3rd step 6 for calculating the blending ratio of plural raw materials so that the states of the intermediate products and the required quantity of heat estimated in the 2nd step 4 fall within respective previously set upper and lower limits, and a 4th step 12 for controlling the quantity of respective raw material to be supplied to the 1st process based on the blending ratio of plural raw materials which is calculated in the 3rd step 6.
    • 46. 发明专利
    • CEMENT PRODUCING DEVICE
    • JPH11246247A
    • 1999-09-14
    • JP5081498
    • 1998-03-03
    • TAIHEIYO CEMENT CORP
    • ANZAI TATSUOOBANA HIROSHIYAMAMOTO YASUSHI
    • C04B7/24C04B7/36C04B7/60
    • PROBLEM TO BE SOLVED: To change a municipal refuse incineration ash, sludge, shell or the like as raw materials into a resource as cement by providing each device for removing a iron chip and water, pulverizing and mixing the raw material, firing and cooling, mixing and pulverizing clinker and gypsum and treating a waste gas to make toxic materials in the raw material non-toxic. SOLUTION: This cement producing device is provided with an incineration ash drying pretreating device, the raw material pulverizing device for pulverizing the incineration ash and lime stone, the compounding and mixing device for the incineration ash and the lime stone, the firing and cooling device for converting to a cement clinker by firing the raw material, the product pulverizing device for mixing and pulverizing clinker and gypsum and if necessary, adding a coagulation adjuster to turn to cement and the waste gas treating device for rapidly cooling the waste gas generated from the firing and cooling device to suppress the re-synthesis of dioxins and to make non-toxic. Alumina and clay are added to the raw materials to adjust SiO2 , Fe2 O3 and Al2 O3 components. The lime stone and the incineration ash are separately pulverized to be compounded. The clinker is obtained by firing the raw material at 1,250-1,450 deg.C.
    • 50. 发明专利
    • METHOD FOR CONTROLLING AND REMOVING HARMFUL SUBSTANCE FROM CEMENT FIRING EQUIPMENT AND DEVICE THEREFOR
    • JPH11130490A
    • 1999-05-18
    • JP30991497
    • 1997-10-24
    • KAWASAKI HEAVY IND LTD
    • KANAMORI SHOZOMURAO MIKIO
    • C04B7/44C04B7/36C04B7/60
    • PROBLEM TO BE SOLVED: To provide a method by which harmful substances such as alkali, chlorine, sulfur and heavy metals can efficiently be removed from a rotary kiln type cement firing equipment through the flow rate control in each of the sections of the equipment and the generation of coatings in various regions of the equipment, such as extracted exhaust gas duct and kiln inlet hood, can be inhibited and also, the ray material loss and heat loss can be reduced and further, the direct fall of a raw material to the kiln inlet can be prevented, to enable always stable continuous operation of the equipment. SOLUTION: This method comprises sampling a preheated raw material to be introduced into a kiln inlet hood 14 to analyze harmful substance contents in the raw material, controlling the flow rate of an exhaust gas portion which is circulated from a cyclone 32 to the kiln inlet hood 14, so that the results of the analyses meet the target values, also, detecting the cyclone inlet gas temp. and controlling the flow rate of cooling air so that the cyclone inlet gas temp. is adjusted to 600 to 800 deg.C, and concurrently, detecting the flow rates of cooling air and another exhaust gas portion which is discharged to the outside of the system from a dust collector 44, and controlling the flow rate of this exhaust gas portion so that the flow rate of the exhaust gas portion is almost equal to that of the cooling air.