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    • 5. 发明授权
    • FCC combustion zone catalyst cooling apparatus
    • FCC燃烧区催化剂冷却装置
    • US4710357A
    • 1987-12-01
    • US764360
    • 1985-08-12
    • Ismail B. CetinkayaDaniel N. Myers
    • Ismail B. CetinkayaDaniel N. Myers
    • B01J8/24C10G11/18B01J8/18
    • B01J8/1809C10G11/182C10G11/187B01J2208/00203B01J2208/0053B01J2208/00548
    • An apparatus for the cooling of hot fluidized solid particles such as catalyst of an FCC petroleum refining process includes a conduit in which particles flow downward from a first dense phase fluidized bed into a cooling chamber and contact the shell side of a vertically oriented shell and tube heat exchanger where cooling occurs via indirect heat exchange with a cooling medium circulating in the tubes. The extent of cooling is controlled by the varying of the heat transfer coefficient between the tubes and particles in the heat exchanger. The coefficient is varied by changing the quantity of fluidizing gas fed to the fluidized bed in the heat exchanger. The heat exchanger is located within a lower portion of the cooling chamber totally below the particle inlet and outlet conduits. The heat exchanger can therefore be removed from service and protected by being buried under unfluidized relatively cool catalyst. The fluidizing gas supports combustion within a lower combustion zone.
    • 用于冷却FCC石油精炼方法的催化剂的热流化固体颗粒的装置包括一个导管,其中颗粒从第一密相流化床向下流到冷却室中,并接触垂直定向的壳和管的壳侧 热交换器,其中通过与在管中循环的冷却介质的间接热交换进行冷却。 冷却的程度由热交换器中的管和颗粒之间的传热系数的变化来控制。 通过改变在热交换器中供给到流化床的流化气体的量来改变系数。 热交换器位于冷却室的下部,完全在颗粒入口和出口管道下方。 因此,热交换器可以从使用中除去并被埋在非流动的相对较冷的催化剂中而被保护。 流化气体支持下燃烧区内的燃烧。
    • 6. 发明授权
    • FCC combustion zone catalyst cooling process
    • FCC燃烧区催化剂冷却过程
    • US4578366A
    • 1986-03-25
    • US687352
    • 1984-12-28
    • Ismail B. CetinkayaDaniel N. Myers
    • Ismail B. CetinkayaDaniel N. Myers
    • B01J20060101B01J8/00B01J8/24B01J38/32C10G20060101C10G11/18B01J21/20
    • B01J8/1809C10G11/182C10G11/187B01J2208/00203B01J2208/00256B01J2208/00292B01J2208/0053B01J2208/00548Y10S208/01
    • A process and apparatus for the cooling of hot fluidized solid particles such as catalyst of an FCC petroleum refining process. The particles flow downward from a first dense phase fluidized bed into a cooling chamber and contact the shell side of a vertically oriented shell and tube heat exchanger where cooling occurs via indirect heat exchange with a cooling medium circulating in the tubes. The extent of cooling is controlled by the varying of the heat transfer coefficient between the tubes and particles in the heat exchanger. The coefficient is varied by changing the quantity of fluidizing gas fed to the fluidized bed in the heat exchanger. The heat exchanger is located within a lower portion of the cooling chamber totally below the particle inlet and outlet conduits. The heat exchanger can therefore be removed from service and protected by being buried under unfluidized relatively cool catalyst. The fluidizing gas supports combustion within a lower combustion zone.
    • 用于冷却热液化固体颗粒如FCC石油精炼方法的催化剂的方法和设备。 颗粒从第一密相流化床向下流入冷却室,并接触垂直取向的管壳式热交换器的壳侧,通过与在管中循环的冷却介质的间接热交换进行冷却。 冷却的程度由热交换器中的管和颗粒之间的传热系数的变化来控制。 通过改变在热交换器中供给到流化床的流化气体的量来改变系数。 热交换器位于冷却室的下部,完全在颗粒入口和出口管道下方。 因此,热交换器可以从使用中除去并被埋在非流动的相对较冷的催化剂中而被保护。 流化气体支持下燃烧区内的燃烧。