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MEMBRANE REACTORS FOR THE FISCHER-TROPSCH SYNTHESIS

机译:费-托合成反应的膜反应器

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摘要

The analysis of the specific features of the Fischer-Tropsch synthesis helps formulating the most important requirements to the FTS reactor. Membrane reactor designs can be useful for the FTS process application. Semi-permeable hydrogen-selective distributors allow to control the H_2:CO ratio along the catalyst bed and thus enhance the selectivity of the process. Membranes of extractor type can help to improve the FTS performance by selective removing water from the reaction volume. On the other hand, plug-through contactor membrane reactor design (PCM) seems to meet all the other requirements, ensuring the high concentration of the catalyst, isothermicity, high gas-liquid interface area, small effective diffusion length and reasonable hydraulic resistance. Varying the membrane composition and conditions of its preparation leads to the changes in porous structure parameters of the PCM membrane. This allows to weaken the diffusion constrains in a predictable way and, therefore, to control the productivity and selectivity of the Fischer-Tropsch process.
机译:费-托合成的特定特征的分析有助于制定对FTS反应器最重要的要求。膜反应器设计可用于FTS工艺应用。半渗透性氢选择性分配器可控制沿着催化剂床层的H_2:CO比率,从而提高了工艺的选择性。萃取器类型的膜可通过从反应体积中选择性除去水来帮助改善FTS性能。另一方面,插入式接触器膜反应器设计(PCM)似乎可以满足所有其他要求,从而确保了催化剂的高浓度,等温性,高的气液界面面积,小的有效扩散长度和合理的水力阻力。改变膜组成及其制备条件会导致PCM膜的多孔结构参数发生变化。这允许以可预测的方式削弱扩散约束,并因此控制费-托工艺的生产率和选择性。

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