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    • 1. 发明申请
    • Multistage compact fischer-tropsch reactor
    • 多级紧凑型费托反应堆
    • US20040102530A1
    • 2004-05-27
    • US10302478
    • 2002-11-22
    • Blue Star Sustainable Technologies Corporation
    • Alessandro G. BorsaNicholas E. Vanderborgh
    • C07C027/06B01J008/04
    • C10G2/341B01J8/065B01J8/067B01J23/8946B01J2208/00203B01J2208/00212B01J2208/0053B01J2219/30
    • A multistage compact packed-bed Fischer-Tropsch reactor comprises a plurality of first-stage reaction tubes and a plurality of second-stage reaction tubes in a reaction-heat-exchange chamber of a reactor vessel. The interior space of each of the reaction tubes contains a packed bed of catalyst. The reactor vessel contains an interstage fluid process chamber and a heat exchanger for condensing hydrocarbon products and water. After passing through catalyst in the first-stage reaction tubes, a process gas stream is cooled by a heat exchanger within the reactor vessel to condense hydrocarbon products and water. The liquid hydrocarbons and water are removed from the reactor vessel. The product gas stream then enters the second-stage tubes in which it is preheated by transfer of heat from the first-stage reaction tubes. The reactor comprises an exit-fluid process chamber within the reactor vessel. After passing through the catalyst in the second-stage reaction tubes, the process gas stream is cooled by a second heat exchanger within the reactor vessel to condense hydrocarbon products and water out of the process gas stream. In the exit-fluid process chamber, liquid hydrocarbons and water are separated from the process gas stream.
    • 多级紧凑型填充床费 - 托反应器包括反应容器的反应 - 热交换室中的多个第一级反应管和多个第二级反应管。 每个反应管的内部空间包含催化剂的填充床。 反应器容器包含级间流体处理室和用于冷凝烃产物和水的热交换器。 在通过第一级反应管中的催化剂之后,通过反应器容器内的热交换器冷却工艺气流以冷凝碳氢化合物产物和水。 将液体烃和水从反应器容器中取出。 产物气流然后通过从第一级反应管传递热量进入其预热的第二级管。 反应器包括反应器容器内的出口流体处理室。 在通过第二级反应管中的催化剂之后,工艺气流由反应器容器内的第二热交换器冷却,以使烃产物和水从工艺气流中冷凝。 在出口流体处理室中,液体烃和水与工艺气流分离。