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    • 2. 发明专利
    • DETECTION METHOD OF QUANTITY OF DUMPED GARBAGE
    • JPH10220724A
    • 1998-08-21
    • JP3325897
    • 1997-01-30
    • NIPPON STEEL CORPNITTETSU PLANT DESIGNING CORP
    • IWAMOTO SHINJIHIDAKA RYOTAHIURA FUMIAKIKAMIYA JUNICHIMATSUMOTO SHUICHI
    • F23G5/44F27B15/08F27B15/20
    • PROBLEM TO BE SOLVED: To enable accurate detection of the quantity of dumped garbage even when the garbage diffusively drops side ways within a vertical part of a dirt supply chute or long-sized dirt hangs from a dirt supplying device by arranging a plurality of amount of dumped garbage sensors as spaced at a specified interval parallel with the direction of dumping the garbage at the dirt supply chute. SOLUTION: Amount of dumped garbage sensors 14, 15 and 16 are all of a photoelectric tube type and are installed in a pair on the light emitting side and on the photodetecting side respectively. The sensors detect light intercepted time while dropping garbage G passes between the two sensors and integrate the detection time to measure a correct amount (volume) of the garbage G passing. The amount of dumped garbage sensors 14, 15 and 16 set the direction of detection parallel with the direction of dumping the garbage and three sets 14, 15 and 16 thereof are installed horizontal to the direction of dumping the garbage G so as to obtain a proper resolving power with respect to the width of the dirt supply chute 12. This can prevent missed and duplicated detection of the dropping garbage G thereby achieving an accurate proportion between the amount of the actually dropping garbage G and an amount of dumped garbage signal.
    • 3. 发明专利
    • JPH05340675A
    • 1993-12-21
    • JP17603092
    • 1992-06-11
    • NIPPON STEEL CORPNITTETSU PLANT DESIGNING CORP
    • TAWARA YOICHIHARAJIRI HACHIROKAMIYA JUNICHIFURUTA MASAKAZUHIURA FUMIAKITANAKA YUKIMASA
    • F27B15/10F27D7/02
    • PURPOSE:To enable burning gaseous fuel in a manner of multifuel combustion in safety, without raising environmental problems, and highly efficiently in a circulating, fluidized bed type combustion chamber with a two-stage supply of air by a method wherein gaseous fuel is fed through a pipe provided inside a secondary air-feeding pipe and a specific relationship is maintained between the amount of secondary air fed through a lower-level inlet and the flow-rate of gaseous fuel. CONSTITUTION:Granular coal 1 and limestone 3 are fed into a fluidized bed combustion chamber 6 by a feed pipe 5 and primary air blown into the fluidized bed combustion chamber 6 by a primary air-feeding pipe 8, which is connected to the bottom of the fluidized bed combustion chamber 6, keeps the granular coal 1, limestone 3, etc., in a fluidized state. A secondary air upper-level feed pipe 9 and a secondary air lower-level feed pipe 24 are connected to the fluidized bed combustion chamber 6 and a gaseous fuel feed pipe 25 is connected to the fluidized bed combustion chamber 6 in a concentric arrangement inside the secondary air lower-level feed pipe 24. Under this piping arrangement the feeding of air and gaseous fuel is made to maintain a relationship between Q1 representing the amount of secondary air at the lower level, i.e., the stream through the secondary air lowerlevel feed pipe 24, and Q2 representing the flow-rate of the gaseous fuel, i.e., the stream through the gaseous fuel feed pipe 25, expressed as Q1/Q2>=0.3A0 where A0 represents a threoretical amount of air for combustion against gaseous fuel.
    • 4. 发明专利
    • METHOD FOR BURNING CHARCOAL MATERIAL BY USING CIRCULATING FLUIDIZED BED
    • JPH0355408A
    • 1991-03-11
    • JP19010189
    • 1989-07-22
    • NIPPON STEEL CORPNITTETSU PLANT DESIGNING CORP
    • TAWARA YOICHIKAMIYA JUNICHIHIURA FUMIAKITANAKA YUKIMASAFUJITA GENJI
    • F23C10/00F23C10/02
    • PURPOSE:To produce quantities of heat through improvement of a ratio of a charcoal material consumed for combustion by a method wherein when combustion gas is discharged to the outside of a system, fly ash, having a specified grain size or more, of fly ash separated away from combustion gas by means of a dust collector is graded and blown in a fluidized bed combustion chamber. CONSTITUTION:Combustion gas is fed to a convection boiler 9 and the heat of which is recovered. After dust is removed from the combustion gas by means of first and second dust collectors 10 and 11, the combustion gas is discharged to the outside of a system by means of a blower 12. In this case, a solid material with a grain size of 2mum or more is separated away from a solid material by means of the first dust collector 10 and fine dust is separated by the second dust collector 11. Fly ash with a grain size of 2mum separated by means of the first dust collector 10 is returned through a coarse grain return pipe 15 to a fluidized bed combustion chamber 2. The coarse grain return pipe 15 is opened in a level higher than that of a secondary air introduction pipe 5 and in the fluidized bed combustion chamber 2. Since this position is a part where the internal pressure of the fluidized bed combustion chamber 2 is comparatively low and oxygen concentration in the fluidized bed combustion chamber 2 is increased by means air blown through the secondary air introduction pipe 5, excellent combustion at an unburnt part located to the central part of fly ash is effected.
    • 5. 发明专利
    • HEAT RECOVERY METHOD FOR CIRCULATING FLUIDIZED BED
    • JPH0355407A
    • 1991-03-11
    • JP19010089
    • 1989-07-22
    • NIPPON STEEL CORPNITTETSU PLANT DESIGNING CORP
    • TAWARA YOICHIKAMIYA JUNICHIHIURA FUMIAKITANAKA YUKIMASAFUJITA GENJI
    • F23C10/00F23C10/02
    • PURPOSE:To enable high-efficient recovery of heat possessed by a solid material without complication of equipment and operation by a method wherein heat is taken out to external part from the thickened part of the solid material formed in the middle of an external circulating route. CONSTITUTION:Combustion gas produced by combustion is raised within a fluidized bed combustion chamber 2 together with dust. Combustion gas away from which dust is separated by means of a cyclone 5 is fed through a discharge pipe 6 to a convection boiler 7. A heat transfer pipe 8 is arranged in the convection boiler 7, and heat possessed by combustion gas flowing through the discharge pipe 6 is recovered by fluid flowing through a heat transfer pipe 8. Meanwhile, a solid material, e.g. an unburnt component, an ash component, separated away from the combustion gas by means of the cyclone 5 is lowered to a return pipe 11. The solid material gathers at a bent part being the lower part of the return pipe to form a particle thickened part 12. A heat transter pipe 14 is arranged to the particle thickened part 12, and since fluid 15, e.g. water, flows, heat possessed by the solid material is transferred to the fluid 15 through the pipe wall of the heat transfer pipe 14 with high efficiency. This constitution simplifies recovery of the heat of the solid material, e.g. an unburnt component, an ash component.