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    • 3. 发明专利
    • Combustion chamber for waste melting facility
    • 用于废物熔化设备的燃烧室
    • JP2005090869A
    • 2005-04-07
    • JP2003325234
    • 2003-09-17
    • Nippon Steel CorpNittetsu Plant Designing Corp新日本製鐵株式会社日鐵プラント設計株式会社
    • KURITA MASAYAFUJITA GENJI
    • F23G5/44F23G5/00F23G5/16F27D17/00
    • PROBLEM TO BE SOLVED: To provide a combustion chamber capable of preventing clinker formation in a burner port of an oil burning burner in regard to a combustion chamber for a waste melting facility.
      SOLUTION: In the combustion chamber 1 arranged with the oil burning burner of an exhaust gas treatment system of the waste melting facility burning exhaust gas from a waste melting furnace, a wall of a burner port 3 in a swirl direction upstream side of combustion gas swirling along with dust in the combustion chamber is extended toward a center of the combustion chamber 1 to form a dust shielding wall 4 shielding the dust, an air blowing pipe 9 is arranged for blowing air for cooling into the burner port, and a cooling piping 10 sending a coolant such as cooling air is embedded in a refractory in a periphery of the burner port.
      COPYRIGHT: (C)2005,JPO&NCIPI
    • 要解决的问题:提供一种燃烧室,其能够防止燃烧燃烧器的燃烧器口中的熟料形成用于废物熔化设备的燃烧室。 解决方案:在燃烧室1中,设置有废气熔化设备的废气处理系统的燃烧燃烧器的燃烧炉,其从废物熔化炉中燃烧废气,燃烧器端口3的壁在涡流方向的上游侧 与燃烧室中的灰尘一起旋转的燃烧气体朝向燃烧室1的中心延伸,形成屏蔽灰尘的防尘屏蔽壁4,布置吹风管9,用于吹送空气以冷却到燃烧器口中, 将诸如冷却空气的冷却剂的冷却管道10嵌入在燃烧器端口的周边的耐火材料中。 版权所有(C)2005,JPO&NCIPI
    • 7. 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.
    • 8. 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.