利索-全球专利检索

  1. 登录
  2. 注册

搜索结果

25 条记录 (耗时 0.031 秒)

    Method and apparatus for processing bed material in fluidized bed reactors
    22.
    发明授权
    Method and apparatus for processing bed material in fluidized bed reactors 失效
    流化床反应器床床处理方法和装置

    公开(公告)号：US5540894A

    公开(公告)日：1996-07-30

    申请号：US66277

    申请日：1993-05-26

    申请人： Timo Hyppanen

    发明人： Timo Hyppanen

    IPC分类号： F23C10/24 ,  B01J20060101 ,  B01J8/18 ,  B01J8/26 ,  B01J8/38 ,  F22B31/00 ,  F23C10/02 ,  F23C10/10 ,  F27B15/14 ,  F27B15/08 ,  F27B15/16

    CPC分类号： F22B31/0092 ,  B01J8/1836 ,  B01J8/26 ,  B01J8/388 ,  F22B31/0084 ,  F23C10/10 ,  B01J2208/00088 ,  B01J2208/00132 ,  B01J2208/00495 ,  F23C2206/101 ,  F23C2206/103

    摘要： Particles in a fluidized bed reactor (e.g. a circulating fluidized bed reactor) are discharged from the reactor chamber and then cooled (heat is recovered from them) in a processing chamber. This is accomplished in a particularly advantageous way by discharging the particles from the reactor chamber at a first level (e.g. through a non-mechanical seal or a classifying wall) into a lifting chamber. Upwardly flowing gas in the lifting chamber entrains the particles and lifts them into the processing chamber. After processing, the particles in the processing chamber are returned to the reactor chamber at level higher than the first level, at which point the pressure in the processing chamber is higher than the pressure in the reactor chamber. The particles may be classified in the lifting chamber by utilizing fluidizing gas to transport solid particles smaller than a predetermined size to the processing chamber while discharging larger particles from the bottom of the lifting chamber.

    摘要翻译： 流化床反应器（例如循环流化床反应器）中的颗粒从反应器室排出，然后在处理室中冷却（从它们回收热量）。 这通过将来自反应器室的颗粒在第一水平（例如通过非机械密封或分级壁）排放到提升室中而以特别有利的方式实现。 提升室中的向上流动的气体夹带着颗粒并将其提升到处理室中。 在处理之后，处理室中的颗粒以高于第一水平的水平返回到反应室，此时处理室中的压力高于反应器室中的压力。 通过利用流化气体将颗粒分类到提升室中，以将小于预定尺寸的固体颗粒输送到处理室，同时从提升室的底部排放较大的颗粒。

    Centrifugal separator in pressure vessel
    23.
    发明授权
    Centrifugal separator in pressure vessel 失效
    压力容器中的离心分离器

    公开(公告)号：US5460788A

    公开(公告)日：1995-10-24

    申请号：US164888

    申请日：1993-12-10

    申请人： Timo Hyppanen ,  Juhani Isaksson ,  Timo Eriksson ,  Teuvo Pulkkinen ,  Steven J. Provol

    发明人： Timo Hyppanen ,  Juhani Isaksson ,  Timo Eriksson ,  Teuvo Pulkkinen ,  Steven J. Provol

    IPC分类号： B01D39/20 ,  B01J8/00 ,  B01J8/24 ,  B01J8/38 ,  B04C5/081 ,  B04C5/28 ,  F23C10/10 ,  F23C10/16 ,  F22B1/00 ,  F27B15/08

    CPC分类号： B01J8/384 ,  B01J8/006 ,  B04C5/081 ,  B04C5/28 ,  F23C10/10 ,  F23C10/16

    摘要： A pressurized fluidized bed reactor is provided utilizing a centrifugal separator having a gas space that is distinctly non-circular, preferably having a circularity of greater than or equal to 1.15. Most desirably the cyclone has a quadrate (e.g. square) cross-section, and is disposed inside of the pressure vessel along with the reactor chamber containing the fluidized bed. A number of ceramic candle or honeycomb filters may be provided connected to the gas outlet from the cyclone separator, within the pressure vessel, to filter the gas. This construction provides a minimized diameter of the pressure vessel because the reactor chamber with square cyclones is more compact than if conventional circular cross-section cyclones are employed. Also a second pressure vessel is not needed for the candle or honeycomb filters since there is sufficient room within the pressure vessel to accommodate them.

    摘要翻译： 使用具有明显非圆形，优选具有大于或等于1.15的圆形度的气体空间的离心分离器来提供加压流化床反应器。 最希望旋风分离器具有方形（例如正方形）横截面，并且与含有流化床的反应器室一起设置在压力容器的内部。 可以在压力容器内连接到旋风分离器的气体出口的多个陶瓷蜡烛或蜂窝过滤器以过滤气体。 这种结构提供了压力容器的最小化直径，因为具有方形旋风分离器的反应室比采用常规圆形横截面旋风分离器更紧凑。 另外，蜡烛或蜂窝过滤器不需要第二压力容器，因为压力容器内有足够的空间来容纳它们。