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    • 75. 发明授权
    • Fast fluidized bed reactor and method of operating the reactor
    • 快速流化床反应器和操作反应器的方法
    • US4548138A
    • 1985-10-22
    • US613267
    • 1984-05-24
    • Jakob Korenberg
    • Jakob Korenberg
    • B01J8/26B01J8/32B01J8/38C10J3/54C10J3/56F23C6/04F23C10/00F23G7/00
    • B01J8/32B01J8/26B01J8/38C10J3/526C10J3/54C10J3/56C10J3/74C10J3/86F23C10/005F23C6/045C10J2300/0916C10J2300/092C10J2300/093C10J2300/0956F23C2206/101F23C2206/103
    • A fast fluidized bed reactor, comprising an upright reaction chamber for containing a bed of granular material, the chamber having a cylindrical upper region and a lower region; a feeder for feeding matter into the lower region; apparatus for supplying pressurized air to the reaction chamber to fluidize the granular material in the circulating regime, whereby a portion of the granular material is entrained into the upper region; apparatus for tangentially supplying pressurized air to the upper region, the second stream of air being supplied, and the reactor being constructed, in a manner to provide a Swirl number of at least 0.6 and a Reynolds number of at least 18,000 in the upper region, thereby creating a cyclone of turbulence; apparatus for separating the granular material and the reaction gases exiting from the reaction chamber and returning the separated granular material to the lower region; a second fluidized bed fluidized in the bubbling regime and situated in the lower region adjacent a partition formed in the lower region for partitioning the circulating fluidized bed from the second fluidized bed, the second fluidized bed fluidizing the granular material separated from the reaction gases and the partition being situated to permit a portion of the granular material from the second fluidized bed to overflow into the circulating bed; and a heat exchanger immersed in the second fluidized bed.
    • 一种快速流化床反应器,包括用于容纳颗粒材料床的直立反应室,所述室具有圆柱形上部区域和下部区域; 用于将物质进料到下部区域的进料器; 用于向反应室供应加压空气以使循环状态下的颗粒物质流化的装置,由此将一部分颗粒材料夹带到上部区域中; 用于向上部区域切向供应加压空气的装置,供应的第二气流和反应器的构造,以在上部区域中提供至少为0.6的漩涡数和至少18000的雷诺数, 从而造成湍流的旋风; 用于分离从反应室排出的颗粒材料和反应气体并将分离的颗粒材料返回到下部区域的装置; 在起泡区域中流化的第二流化床,并且位于邻近形成在下部区域中的隔板的下部区域中,用于将循环流化床与第二流化床分隔开,第二流化床使从反应气体分离的颗粒材料流化, 分隔件位于允许来自第二流化床的一部分颗粒材料溢出到循环床中; 和浸入第二流化床中的热交换器。
    • 76. 发明授权
    • Fast fluidized bed reactor and method of operating the reactor
    • 快速流化床反应器和操作反应器的方法
    • US4457289A
    • 1984-07-03
    • US370248
    • 1982-04-20
    • Jakob Korenberg
    • Jakob Korenberg
    • B01J8/24B01J8/32F22B31/00F23C3/00F23C9/06F23C10/02F23C10/28F23G5/14F23G5/30F23G5/46F23J15/00F27B15/00F27B15/10F22B1/00
    • B01J8/32F22B31/0053F22B31/0084F22B31/0092F23C10/02F23C3/006F27B15/10
    • A method of operating a fast fluidized bed reactor according to the invention comprises: (1) providing a fluidized bed reactor having an upper and a lower region, the upper region having a cylindrical shape; (2) feeding matter to be reacted into the lower region of the reactor; (3) supplying a first stream of pressurized air to the reactor in the lower region at a velocity to fluidize the granular material in the circulating regime, a portion of the granular material is continually entrained into the upper region; (4) tangentially supplying a second stream of pressurized air to the upper region wherein, at maximum operating capacity for the reactor, the second stream of air constitutes in excess of about 50% of the total pressurized air fed to the reactor; (5) maintaining a Swirl number of at least about 0.6 and a Reynolds number of at least about 18,000 in the upper region for providing a cyclone of turbulence which increases the rate of reaction in the reactor; and (6) permitting the reaction gases in the upper region to exit from the reactor through an exit throat, while retaining substantially all of the granular material within the reactor. In accordance with the invention, cyclone particle separators are not required.Apparatus suitable for use in practicing the above-recited method are also disclosed.
    • 根据本发明的操作快速流化床反应器的方法包括:(1)提供具有上部和下部区域的流化床反应器,上部区域具有圆柱形形状; (2)将要反应的物质进料到反应器的下部区域; (3)在下部区域以一定的速度向第一反应器供应第一加压空气流,以使颗粒状物质在循环状态下流化,一部分颗粒状物料连续地夹带在上部区域中; (4)向上部区域切向地供应第二加压空气流,其中在反应器的最大工作能力下,第二空气流构成超过供给到反应器的总加压空气的约50%; (5)在上部区域保持至少约0.6的漩涡数和至少约18,000的雷诺数,以提供湍流的旋流器,其增加反应器中的反应速率; 和(6)允许上部区域中的反应气体通过出口喉管从反应器中排出,同时将基本上所有的颗粒材料保持在反应器内。 根据本发明,不需要旋风分离器颗粒分离器。 还公开了适用于实施上述方法的装置。
    • 79. 发明授权
    • Fluidized bed systems
    • 流化床系统
    • US4276062A
    • 1981-06-30
    • US798544
    • 1977-05-19
    • David LyonGerald Moss
    • David LyonGerald Moss
    • F23C10/22B01J8/00B01J8/32F23C10/00F23C10/10F23G5/30F27B15/00B01D53/12
    • F23C10/10B01J8/005B01J8/32Y10S48/04
    • A selected fraction of solid particles having sizes, densities and/or weights in a selected range is separated from a mixture of articles by fluidizing the mixture in a bed using a fluidizing fluid to cause particles including the selected fraction to pass out of the top of the bed; conveying the particles in a conveying fluid to a suitable separator (e.g. a cyclone) wherein the selected particles fraction is separated from smaller, lighter particles; injecting the separated fraction from the separator into a utilization zone (e.g. a fluid bed reactor); entraining other particles in the conveying fluid to another separator (e.g. a cyclone) to produce solids-free conveying fluid which is recirculated for re-use. The original particles mixture may be obtained by separation (e.g. in a cylone) from fluid leaving the utilization zone.
    • 通过使用流化流体使床中的混合物流化,将选定范围内的尺寸,密度和/或重量的选定部分的固体颗粒与制品的混合物分离,以使包括所选部分的颗粒从 床; 将输送流体中的颗粒输送到合适的分离器(例如旋风分离器),其中所选择的颗粒馏分与较小的较轻颗粒分离; 将分离的馏分从分离器注入利用区(例如流化床反应器)中; 将输送流体中的其他颗粒夹带到另一分离器(例如旋风分离器)中以产生无固体的输送流体,其被再循环以供再利用。 原始颗粒混合物可以通过从离开使用区域的流体中分离(例如在环形酮中)获得。
    • 80. 发明授权
    • Operating method
    • 操作方法
    • US4084545A
    • 1978-04-18
    • US803831
    • 1977-06-06
    • Herman NackKe-Tien Liu
    • Herman NackKe-Tien Liu
    • C04B2/02B01D53/14B01J8/32B01J8/38C01F1/00C01G49/02C01G53/04F22B1/02F22B31/00F23C10/00F23C10/02F23C10/08F23C10/10F23G5/30F27B15/00F23D1/00
    • F23C10/10B01J8/32B01J8/388F22B31/0084F23C2206/101F23C2206/103
    • A method of operating a fluidized bed system, typically as a combustor system for power or steam generation by burning high-sulfur coal, which comprises forming an entrained fluidized bed in a first space region containg a first solid bed particle component, such as a hematite ore containing over 90% Fe.sub.2 O.sub.3, or limestone, forming in a more limited space region within the first region a dense fluidized bed containing a second solid bed particle component, such as larger particles of the hematite, essentially comprising a material having long-term physical and chemical stability in the fluidized bed system so as to be substantially non-agglomerating and not subject to substantial attrition therein, providing a recirculation path such as through a cyclone separator and particle reservoir for the first particle component from the first space region through the dense fluidized bed in the more limited space region, and operating the fluidized bed system at a velocity such that the second component particles are effectively retained in the dense fluidized bed in the more limited space region, whereas the first component particles recirculate and interpenetrate therethrough, commingling with the second component particles.
    • 一种操作流化床系统的方法,通常是通过燃烧高硫煤作为用于发电或蒸汽的燃烧器系统,其包括在包含第一固体床颗粒组分如赤铁矿的第一空间区域内形成夹带的流化床 含有超过90%的Fe 2 O 3或石灰石的矿石在第一区域内在更有限的空间区域中形成含有第二固体床颗粒组分的致密流化床,例如赤铁矿的较大颗粒,基本上包括具有长期物理 和在流化床系统中的化学稳定性,以便基本上非附聚并且不会在其中大量磨损,从而提供再循环路径,例如通过旋流分离器和用于第一颗粒组分的颗粒储存器从第一空间区域通过致密的 在更有限的空间区域中的流化床,并以使得第二组合物的速度操作流化床系统 有效颗粒被有效地保留在更有限的空间区域中的致密流化床中,而第一组分颗粒再循环并贯穿其中,与第二组分颗粒混合。