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    • 3. 发明授权
    • Internal circulating fluidized bed type boiler and method of controlling
the same
    • 内循环流化床式锅炉及其控制方法
    • US5138982A
    • 1992-08-18
    • US760858
    • 1991-09-17
    • Takahiro OhshitaTsutomu HigoShigeru KosugiNaoki InumaruHajime Kawaguchi
    • Takahiro OhshitaTsutomu HigoShigeru KosugiNaoki InumaruHajime Kawaguchi
    • B01J8/18F22B31/00F23C10/00F23C10/06F23C10/14F23G5/30
    • B01J8/1818F22B31/0061F22B31/0092F23C10/005F23C10/06F23C10/14F23G5/30B01J2208/00141
    • An internal recycling type fluidized bed boiler includes a primary fluidized bed incinerating chamber constructed by an air diffusion plate, and an inclined partition wall provided above a portion of the diffusion plate where the mass flow of the air injected from the diffusion plate is greater than that from another portion so as to interfere with the upward flow of the fluidizing air injected from that portion and deflect it towards the portion above the diffusion plate where the mass flow of gas injected is smaller. A thermal energy recovery chamber is formed between the inclined partition wall and a side wall of an incinerator. The inclined partition wall is inclined by 10.degree.-60.degree. relative to the horizontal and is arranged such that the length of its projection in the horizontal direction is 1/6-1/2 of the horizontal length of the bottom of the incinerator bottom. A method of controlling the above fluidized bed boiler with respect to the amount of thermal energy recovered from the thermal energy recovery chamber includes regulating the amount of air injected from a diffuser in the thermal energy recover chamber, based on demands from the user side utilizing the recovered thermal energy. The amount of fuel to the primary fluidized bed incinerating chamber is controlled based on the temperature in the primary fluidized bed incinerating chamber.
    • PCT No.PCT / JP87 / 00530 Sec。 371 1990年1月4日第 102(e)日期1990年1月4日PCT PCT 1987年7月20日PCT公布。 出版物WO89 / 00659 日本1989年1月26日。内部回收型流化床锅炉包括由空气扩散板构成的一级流化床焚烧室,以及设置在扩散板的一部分上方的倾斜分隔壁, 扩散板大于来自另一部分的扩散板,以便干扰从该部分注入的流化空气的向上流动并将其偏转到扩散板上方的部分,其中注入的气体的质量流量较小。 在倾斜分隔壁和焚烧炉侧壁之间形成热能回收室。 倾斜分隔壁相对于水平面倾斜10°-60°,其水平方向的长度为焚烧炉底部底部水平长度的1 / 6-1 / 2。 控制上述流化床锅炉相对于从热能回收室回收的热能量的方法包括:根据来自用户侧的需求调节在热能回收室中从扩散器喷出的空气量, 回收热能。 基于初级流化床焚烧室中的温度控制到初级流化床焚烧室的燃料量。
    • 8. 发明授权
    • Automatic bread producing machine
    • US5887512A
    • 1999-03-30
    • US918803
    • 1997-08-26
    • Yasuhiro KakimotoTakahiro OhshitaNoriyuki Yamamoto
    • Yasuhiro KakimotoTakahiro OhshitaNoriyuki Yamamoto
    • A21B7/00A47J27/00
    • A21B7/005
    • An automatic bread producing machine includes, in a baking chamber, a vessel unit having a bread vessel where a mixing vane for mixing bread ingredients is rotatably provided and a cylindrical bread vessel support fixed to an underside of the bread vessel. The bread vessel support has stoppers formed on the lower circumference thereof. The machine further includes a vessel mounting support mounted at the bottom of the baking chamber for receiving therein the bread vessel support. The vessel mounting support has cutouts formed at its circumferential wall for receiving and firmly holding the stoppers, respectively. Recessed portions are further formed at the circumferential wall of the vessel mounting support for guiding the stoppers to positions adjacent to the corresponding cutouts, respectively. Each cutout is provided adjacent to a lower end of the recessed portion and at one side of the recessed portion located in a rotation direction of the mixing vane. Each stopper is automatically received and locked in position in the corresponding cutout due to a rotation force of the mixing vane so that the vessel unit is automatically fixed relative to the vessel mounting support. While the stoppers are locked in position, an upper surface of each stopper engages with an upper wall surface of the corresponding cutout. The upper surfaces of each stopper and cutout are so shaped as to urge the vessel unit downward during rotation of the mixing vane.
    • 10. 发明授权
    • Composite recycling type fluidized bed boiler
    • 复合循环型流化床锅炉
    • US5156099A
    • 1992-10-20
    • US445679
    • 1989-11-29
    • Takahiro OhshitaShuichi NagatoNorihisa Miyoshi
    • Takahiro OhshitaShuichi NagatoNorihisa Miyoshi
    • F22B31/00F23C10/02F23G7/00
    • F22B31/0084F22B31/0092F23C10/02
    • An internal recycling type fluidized bed boiler in which a fluidized bed portion of the boiler is divided by a partition into a primary combustion chamber and a thermal energy recovery chamber, at least two kinds of air supply chambers are provided below the primary combustion chamber, one for imparting a high fluidizing speed to a fluidizing medium and the other for imparting a low fluidizing speed thereto, thereby providing a whirling and circulating flow to the fluidizing medium in the primary combustion chamber. The fluidizing medium is moved downward in a moving bed in the thermal energy recovery chamber. Thermal energy recovery from exhaust gas is effected in a free board portion or downstream thereof, the cooled exhaust gas being guided to a cyclone, and fine particulate char collected at the cyclone is returned directly above or into a descending moving bed of the fluidizing medium in the primary combustion chamber and/or the thermal recovery chamber, whereby the char will not be immediately scattered to the free board portion and the char is sufficiently precipitated and it is possible to reduce NOx generated by combustion of coal or the like, in the bed.
    • PCT No.PCT / JP89 / 00883 Sec。 371日期:一九八九年十一月二十九日 102(e)1989年11月29日PCT PCT 1989年8月30日PCT公布。 出版物WO90 / 02293 日本1990年8月3日。一种内部回收型流化床锅炉,其中锅炉的流化床部分被隔板分成初级燃烧室和热能回收室,至少提供两种供气室 在主燃烧室下面,一个用于赋予流态化介质高的流化速度,另一个用于赋予低流化速度,从而为主燃烧室中的流化介质提供旋转和循环流。 流化介质在热能回收室的移动床中向下移动。 废气中的热能回收在自由板部分或其下游进行,冷却后的废气被引导至旋风分离器,并且在旋风分离器处收集的细小颗粒焦炭直接返回到流化介质的下降移动床的上方或下方 主燃烧室和/或热回收室,由此该焦炭不会立即散布到自由板部分,并且焦炭充分沉淀,并且可以减少床等中燃烧产生的NOx 。