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公开(公告)号:US06814940B1
公开(公告)日:2004-11-09
申请号:US09623018
申请日:2000-10-30
IPC分类号: B01J818
CPC分类号: B01J8/0055 , B01J8/1854 , B01J8/26 , C10B49/22 , C10B53/00 , C10B53/02 , Y02E50/14 , Y02P20/145
摘要: 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.
摘要翻译: 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。