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    • 1. 发明专利
    • Exhaust gas treatment method and apparatus therefor
    • 排气处理方法及其设备
    • JP2003320211A
    • 2003-11-11
    • JP2002127962
    • 2002-04-30
    • Kawasaki Heavy Ind Ltd川崎重工業株式会社
    • TAKADA TOMOAKI
    • F01N3/02B01D46/38B01D53/94F01N3/08F01N3/24F01N3/28
    • PROBLEM TO BE SOLVED: To provide a high performance exhaust gas treatment method for efficiently removing PM (particulate matter) contained in exhaust gas, and to make an exhaust gas treatment apparatus compact, simple and inexpensive. SOLUTION: The exhaust gas treatment apparatus has an apparatus main body, in which a particle bed 10 comprising particles for capturing particulates contained in exhaust gas, a gas dispersion plate 12 provided under the particle bed, the wind box 6 under the gas dispersion plate and a scattering preventing plate 18 above the particle bed are provided, and the exhaust gas is introduced from the area under the gas dispersion plate 12 to bring the particle bed 10 to a fluidized bed and particulates in the exhaust gas are captured while passing treated gas to the area above the particle bed to discharge the same. A heating member 22 having air permeability is provided to the undersurface of the gas dispersion plate 12. COPYRIGHT: (C)2004,JPO
    • 要解决的问题:为了提供一种高效排除废气中所含的PM(颗粒物质)的废气处理方法,使排气处理装置紧凑,简单,便宜。 解决方案:废气处理装置具有装置主体,其中包括用于捕获废气中所含微粒的颗粒的颗粒床10,设置在颗粒床下方的气体分散板12,气体下方的风箱6 提供了分散板和颗粒床上方的散射防止板18,并且从气体分散板12下方的区域引入废气以使颗粒床10进入流化床,并且废气中的颗粒在通过时被捕获 处理气体到颗粒床上方的区域排出。 具有透气性的加热构件22被提供到气体分散板12的下表面。版权所有(C)2004,JPO
    • 5. 发明专利
    • METHOD FOR BURNING REFUSE AND APPARATUS THEREFOR
    • JPH09280527A
    • 1997-10-31
    • JP11430496
    • 1996-04-10
    • KAWASAKI HEAVY IND LTD
    • TAKADA TOMOAKI
    • F23G5/30F23G5/16F23G5/32F23G7/00
    • PROBLEM TO BE SOLVED: To restrict production of hydrogen chloride gas and dioxin in a two stage combustion refuse incinerator, reduce the amount of volatilization of a heavy metal, and further reduce coating by chloride, and produce high temperature water vapor. SOLUTION: A two stage combustion gas refuse incinerator includes a fluidized layer gasifying furnace which takes an alkali metal oxide and an alkaline earth metal oxide as a fluid medium. Unburned gas from a fluidized gasifying furnace 10 of the two stage combustion gas refuse incinerator is introduced into a cyclone 20 and ash containing unburned carbon, inorganic chloride, and heavy metal are captured, and thereafter the ash is rinsed in a washing apparatus 24 whereby at least a part of the inorganic chloride and at least a part of the heavy metal are dissolved into water. Thereafter, the ash containing unburned carbon after washed is introduced into a later stage combustion furnace 12 and is mixed and burned with the unburned gas from the gasifying furnace 10. Washed waste water containing the inorganic chloride and the heavy metal is used as mixed water for solidifying ash.
    • 6. 发明专利
    • CENTRIFUGAL FLUIDIZED BED DENITRATION APPARATUS
    • JPH09276661A
    • 1997-10-28
    • JP11430396
    • 1996-04-10
    • KAWASAKI HEAVY IND LTD
    • TAKADA TOMOAKITSUTSUMI KAZUOKAWAMURA TARO
    • B01D53/56B01D53/74B01D53/86B01D53/94B01J8/38B01J23/40
    • PROBLEM TO BE SOLVED: To enhance a dehydration ratio and to prevent the clogging of a gas diffusion plate and a fluidized bed with unburned carbon by providing an oxide catalyst layer to at least the outer surface of the gas diffusion plate. SOLUTION: The inner cylindrical surface of a fluidized bed reactor 14 is set to a gas diffusion plate 16 and shield end plates 18, 20 are attached to both ends of the gas diffusion plate 16. An oxide catalyst layer 40 composed of an oxide catalyst such as Pt or Pd is formed on the outer surface of the gas diffusion plate 16. When an engine starts, an exhaust pipe 24 is rotated and the fluidizing particles 22 in the fluidized bed reactor 14 are fluidized by centrifugal force so as to be stuck to the inner surface of the gas diffusion plate 16 and exhaust gas introduced from an introducing pipe 10 at the same time passes through the gas diffusion plate 16 to enter the reactor 14 to fluidize the fluidizing particles 22 and soot is collected in the gaps between the particles. When the exhaust gas comes into contact with the oxide catalyst layer 40, NO2 in the exhaust gas is oxidized to NO2 and a part of unburned carbon or the greater part thereof is oxidized to CO2 and, further NO2 is reacted with unburned carbon to be decomposed into N2 and CO2 .