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    • 1. 发明授权
    • Process for pyrolyzing carbonaceous feedstocks
    • 热解碳质原料的方法
    • US06814940B1
    • 2004-11-09
    • US09623018
    • 2000-10-30
    • Jyrki HiltunenSteven GustJukka-Pekka Nieminen
    • Jyrki HiltunenSteven GustJukka-Pekka Nieminen
    • B01J818
    • B01J8/0055B01J8/1854B01J8/26C10B49/22C10B53/00C10B53/02Y02E50/14Y02P20/145
    • The present invention concerns a process and an apparatus for thermal conversion of biomass and organic wastes. According to the invention, the feedstock is fed into a fluidized-bed reactor, wherein the feed is converted at an elevated temperature under the influence of particulate matter kept in a fluidized state by a fluidizing gas, the particulate matter is transferred from the reactor to a regenerator for regeneration and then recirculated to the reactor after the regeneration, and the converted hydrocarbon products are recovered from the reactor. Both the reactor and the regenerator comprise risers having an axially annular cross section and being equipped with multi-inlet cyclones for the separation of particulate matter. By means of the invention, it is possible to producer pyrolysis oil, the quality of which is higher than that of oil produced with the processes of the prior art. The incorporation of multi-inlet cyclones into the reactor configuration reduces gas velocities, reduces the physical size of the cyclone and shortens the residence time of gases in the cyclone.
    • 本发明涉及用于生物质和有机废物的热转化的方法和装置。 根据本发明,将原料进料到流化床反应器中,其中进料在升高的温度下在流化气体保持在流化状态的颗粒物质的影响下转化,颗粒物质从反应器转移到 用于再生的再生器,然后在再生之后再循环到反应器中,并且将转化的烃产物从反应器中回收。 反应器和再生器都包括具有轴向环形横截面并具有用于分离颗粒物质的多入口旋风分离器的提升管。 通过本发明,可以生产热解油,其质量高于用现有技术方法生产的油的质量。 将多入口旋风分离器并入反应器构型可降低气体速度,减小旋风分离器的物理尺寸并缩短气体在旋风分离器中的停留时间。
    • 4. 发明授权
    • Fluidized bed reaction design
    • 流化床反应设计
    • US06719952B1
    • 2004-04-13
    • US09507605
    • 2000-02-21
    • Wen-Ching YangDavid F. McLaughlinTimothy L. Francis
    • Wen-Ching YangDavid F. McLaughlinTimothy L. Francis
    • B01J818
    • B01J8/1818B01J8/245C01G25/04
    • A fluidized bed reactor (10) for chemically transforming reactants to generate a desired product, having a hollow, elongated, vertically oriented reactor housing (12) for confining the reaction and an unobstructed collection path (18) below the reaction zone for funneling the residue of the process to an exit port (32). A central gas inlet (22) proximate the bottom of the reaction zone within the housing directs gas parallel to the vertical axis of the housing to maintain the raw materials in suspension. A plurality of individually controlled peripheral gas jets (24) positioned at least two elevations along the elongated dimension of the reaction housing (12), and located circumferentially around the housing (12) at each elevation, introduce gas at an angle to promote mixing of the entrained materials in suspension. The clog-free collection path (18) below the reaction zone funnels the residue of the process to an exit port (32) where it is continuously removed by a screw feeder (34). A gas sparger (30) below the reaction zone diverts fine agglomerates of the residue back into the reaction stream to increase the efficiency of the process and minimize the residue.
    • 一种用于化学转化反应物以产生所需产物的流化床反应器(10),其具有用于限制反应的中空的细长的垂直取向的反应器壳体(12)和在反应区下方的无障碍的收集路径(18),用于将残余物 的进程到出口(32)。 邻近壳体内的反应区底部的中心气体入口(22)引导气体平行于壳体的垂直轴线,以保持原料悬浮。 多个独立控制的外围气体射流(24)沿着反应壳体(12)的细长尺寸定位至少两个高度,并且在每个高度处围绕壳体(12)周向定位,以一定角度引入气体以促进混合 夹带的物料悬浮。 在反应区下方的无堵塞的收集路径(18)将该过程的残留物漏出到出口(32),在该出口处被螺旋进料器(34)连续地移除。 反应区下方的气体分布器(30)将残留物的细小附聚物转移回反应物流中,以提高该方法的效率并使残余物最小化。