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    • 104. 发明专利
    • JPH05240416A
    • 1993-09-17
    • JP7314692
    • 1992-02-25
    • EBARA CORP
    • KAMISADA MASAJINAGATOU SHIYUUICHIOSHITA TAKAHIROSATO KEIICHI
    • F23G5/14F23G5/30
    • PURPOSE:To minimize the scattering of unburnt carbon and a fluid medium and control an unburnt gas to be generated to a minimum level in an incinerator. CONSTITUTION:In an incinerator 10 wherein a combustion gas generated from a fire grate part or a fluidized sand bed part 12 is introduced into an upper combustion chamber and mixed with secondary air to complete combustion, the combustion chamber comprises: a recessed portion 14 provided on the way of a gas flow passage, which is recessed laterally with respect to a gas stream and expanded again at a fixed distance; a first barrier 16 formed into a hat shape and provided at the outlet of the recessed portion; a lower combustion chamber 13 provided underneath the barrier and an upper combustion chamber 15 provided above the barrier; and a gas passage 17 provided on the outer side of the barrier. Further, a plurality of secondary air blowing ports 22b for injecting secondary air in a direction opposed to, or cross to, the combustion gas stream from the outlet of the barrier are provided in the upper combustion chamber and, according to this combustion, the stream of the combustion gas is turned in the downstream direction by the secondary air in the upper combustion chamber 15. Furthermore, a second comb-like barrier 23 is provided so that the secondary air and an unmixed combustion gas impact against the second barrier and are mixed with each other in the upper combustion chamber.
    • 105. 发明专利
    • HEAT RECOVERY CONTROL METHOD FOR FLUIDIZED BED BOILER
    • JPH02290402A
    • 1990-11-30
    • JP11132889
    • 1989-04-28
    • EBARA CORP
    • INUMARU NAOKIOSHITA TAKAHIROKOSUGI SHIGERUNAGATOU SHIYUUICHIMIYOSHI YOSHIHISA
    • F23C10/28F22B1/02F23G5/50
    • PURPOSE:To finely control an amount of recovered heat throughout a wide range in a way that a diffusion airflow diffused from a plurality of diffusing devices is controlled classified by the diffusing device by a method wherein a plurality of fluidized bed combustion furnaces are provided, and a plurality of the diffusing devices are mounted to a plurality of heat recovery parts mounted in a fluidized bed and the fluid medium layer of the fluidized bed combustion furnace. CONSTITUTION:A boiler comprises a combination coal and waste combustion fluidized bed combustion bed A, a mono-coal combustion fluidized bed combustion furnace B, and a boiler part C. Heat recovery chambers 114 and 115 are provided in the fluid medium layers of the combination coal and waste combustion fluidized bed combustion furnace A and the mono-coal combustion fluidized bed combustion furnace B. Main diffusing devices 119, 120, 119a, and 120a are arranged to the bottom part in the fluid medium layer of the heat recovery chambers 114 and 115, and auxiliary diffusing devices 121 and 122 are arranged on the side positioned opposite to the main diffusing devices 119 and 120. The large volumes of the heat recovery chambers 114 and 115 are controlled by means of a diffusion airflow independently diffused from the main diffusing devices 119, 120, 119a, and 120a and the auxiliary diffusing devices 121 and 122, resulting in the possibility to finely control heat recovery.
    • 107. 发明专利
    • FLUIDIZED BED TYPE HEAT REACTION EQUIPMENT
    • JPS63131916A
    • 1988-06-03
    • JP27526686
    • 1986-11-20
    • EBARA CORP
    • INUMARU NAOKIHIGO TSUTOMUOSHITA TAKAHIROKOSUGI SHIGERU
    • F23G5/30
    • PURPOSE:To improve the efficiency of reaction and combustion with the effective dispersion of granular solids along a swirl in a fluidized bed by installing the opening pipe ends of an air flow transfer pipe for the granular solids at the bottom of the fluidized bed inside near the boundaries between a part where the flow rate of blown air is relatively small and a part where large. CONSTITUTION:Granular solids supplied into an air flow transfer pipe 37 are mixed with air and then supplied into the inside of a fluidized bed from supply nozzles 39 through the pipe 37. The nozzles 39 are placed near respective houndaries between the air chamber 15, 16 and 16, 17, and the granular solids supplied from there are dispersed into the inside of the swirl fluidized bed along the stream of flowing mediums in an arrow direction. It is sufficient to install the nozzles 39 at two places. As the supply locations of the granular solids are set at the boundary range between a descent moving bed and an ascent moving bed where the mediums are transferred from the lower part of the descent moving bed to the lower part of the ascent moving bed, the granular solids supplied are involved in a swirl to be dispersed wholly into the fluidized bed.
    • 109. 发明专利
    • UNBURNT ASH RECOVERING DEVICE
    • JPS6387520A
    • 1988-04-18
    • JP22980386
    • 1986-09-30
    • EBARA CORP
    • HIGO TSUTOMUOSHITA TAKAHIROKOSUGI SHIGERUINUMARU NAOKI
    • F23J3/06F23C10/24
    • PURPOSE:To improve the combustion rate due to return ashes by providing in parallel a plurality of separation mechanisms with dampers in a combustion waste gas flowpath and adjusting the number of opening and closing of separators to make constant the draft pressure loss of the combustion waste gas in the separation mechanisms. CONSTITUTION:A plurality of separation mechanisms consisting of combinations of separators 7 and dampers 7a are provided in parallel to each other in the combustion waste gas flowpaths of a fluidized bed boiler 1. By this constitution, the waste gas passes through separators 7 and dampers 7a and is sent to a dust collector 8 and dusts and dirts are arrested. Upon this occasion, the control of opening and closing of respective damper 7a is carried out so that by the difference in pressure between the front part and the rear part of the separation mechanism detected by a differential pressure meter 30, the draft pressure loss becomes constant. Thus, it is possible to maintain the ability meeting the waste gas flow rate and to operate the device in a high efficiency zone.