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    • 7. 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。