Fluid bed reactor
    1.
    发明授权
    Fluid bed reactor 失效
    流化床反应器

    公开(公告)号:US5876679A

    公开(公告)日:1999-03-02

    申请号:US833658

    申请日:1997-04-08

    摘要: A fluid bed reactor is provided having a grid baffle structure to provide increased theoretical stages within the reactor to enable the reactor to be used for time/temperature dependent reactions requiring a number of mixing stages and/or an increased particle residence time. The preferred baffle structure comprises a plurality of staggered first and second vertical members extending partly across the reactor from opposed sides of the reactor which form a path for the feed to travel therethrough from the inlet to the outlet of the reactor with the vertical members having vertical cross-members, preferably shorter than the vertical members, extending completely between adjacent vertical members and/or partly in the space between the members to form reaction stage sections whereby feed entering the reactor moves in a serpentine path and/or a sequential underflow and/or overflow path through the reaction stage sections of the baffle from the inlet of the reactor to the reactor outlet.

    摘要翻译: 提供了一种流化床反应器,其具有栅格挡板结构,以在反应器内提供增加的理论级,以使反应器能够用于需要多个混合阶段和/或增加的颗粒停留时间的时间/温度依赖性反应。 优选的挡板结构包括多个交错的第一和第二垂直构件,部分地跨越反应器从反应器的相对侧延伸,其形成用于进料从反应器的入口到出口穿过的路径,垂直构件具有垂直 横向构件,优选地比垂直构件短,在相邻的垂直构件之间和/或部分地在构件之间的空间中完全延伸,以形成反应台段,由此进入反应器的进料以蛇形路径和/或顺序下溢和/ 或溢流路径通过挡板的反应段部分从反应器的入口到反应器出口。

    Firing liquid and gaseous fuels for a circulating fluidizing bed reactor
    2.
    发明授权
    Firing liquid and gaseous fuels for a circulating fluidizing bed reactor 失效
    为循环流化床反应器燃烧液体和气体燃料

    公开(公告)号:US5441406A

    公开(公告)日:1995-08-15

    申请号:US397557

    申请日:1995-03-02

    IPC分类号: F23C5/00 F23C10/10 F27B19/00

    CPC分类号: F23C5/00 F23C10/10

    摘要: A method and system for introducing combustion gases to the upper portion of the dense phase or transition portion of a circulating fluidized bed reactor. The combustion gases are produced in a burner external to the dense phase portion of the reactor wherein the burner receives a mixture of liquid or gaseous fuel and air so as to initiate and maintain combustion within the burner. The combustion gases are then quenched prior to entering the dense phase portion of the reactor so as to reduce the temperature of the combustion gases thereby preventing overheating or sintering of the particulate and significant oxidation reduction in the dense phase portion of the reactor.

    摘要翻译: 一种用于将燃烧气体引入循环流化床反应器的致密相或过渡部分的上部的方法和系统。 燃烧气体在反应器的密相部分外部的燃烧器中产生,其中燃烧器接收液体或气体燃料和空气的混合物,以便启动并保持燃烧器内的燃烧。 然后在进入反应器的密相部分之前将燃烧气体淬灭,以便降低燃烧气体的温度,从而防止颗粒的过热或烧结并且在反应器的致密相部分中显着的氧化还原。

    Solids mixing method
    3.
    发明授权
    Solids mixing method 失效
    固体混合法

    公开(公告)号:US08062393B2

    公开(公告)日:2011-11-22

    申请号:US12286809

    申请日:2008-10-02

    IPC分类号: C01B3/36 C10J3/54 C10L1/00

    摘要: A process for providing fast pyrolysis or gasification of feed material, such as biomass, by mixing it with inert inorganic hot solids in a fluidized mixer/reactor and utilizing released gas from the resulting reaction to transport the mixture from the mixer/reactor.

    摘要翻译: 通过将其与惰性无机热固体在流化混合器/反应器中混合并利用所得反应的释放气体将混合物从混合器/反应器输送来提供诸如生物质的进料的快速热解或气化的方法。

    Solids mixing method
    4.
    发明申请
    Solids mixing method 失效
    固体混合法

    公开(公告)号:US20100083576A1

    公开(公告)日:2010-04-08

    申请号:US12286809

    申请日:2008-10-02

    IPC分类号: C10J3/00

    摘要: A process for providing fast pyrolysis or gasification of feed material, such as biomass, by mixing it with inert inorganic hot solids in a fluidized mixer/reactor and utilizing released gas from the resulting reaction to transport the mixture from the mixer/reactor.

    摘要翻译: 通过将其与惰性无机热固体在流化混合器/反应器中混合并利用所得反应的释放气体将混合物从混合器/反应器输送来提供诸如生物质的进料的快速热解或气化的方法。

    Ash classifier
    5.
    发明授权
    Ash classifier 失效
    灰分类器

    公开(公告)号:US4700636A

    公开(公告)日:1987-10-20

    申请号:US922365

    申请日:1986-10-23

    CPC分类号: F23C10/26 B01J8/005

    摘要: Apparatus is provided for withdrawing a stream of relatively static bed material from an operating fluidized bed reactor and gravity feeding it through a conduit to an exterior classifying chamber into which a downward flow of air is introduced. The airflow is turned in the classifier to move in an upward direction countercurrent to the flow of bed material. The velocity of the air is such that coarse bed material passes downwardly through the airflow and accumulates in the classifying chamber, while the fines are entrained in the upwardly moving airflow and both air and fines are introduced into the fluidized bed reactor.