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Combination of a Two-Zone Fluidized Bed Reactor with a Pd hollow fibre membrane for catalytic alkane dehydrogenation

机译:两区流化床反应器与Pd中空纤维膜的组合用于催化烷烃脱氢

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摘要

The combination of a Pd hollow fibre membrane with a Two-Zone Fluidized Bed Reactor (TZFBR) is described for catalytic dehydrogenation of propane. This configuration aims to combine the in situ catalyst regeneration provided by the TZFBR with the increased conversion that can be achieved with a Pd membrane, which removes hydrogen from the reactor, thus enhancing the reaction rate and in theory allowing even higher than equilibrium conversion. The experiments show that the Pd hollow fibre membrane acts effectively removing hydrogen from the reaction media and that with a Pt-Sn/Al2O3 catalyst the TZFBR can achieve steady state operation in spite of the increased coking of the catalyst. However, with this catalyst the quicker coke formation caused by the removal of hydrogen outweighs the beneficial effect of hydrogen removal and the yield achievable for a given feed is lower in the presence of the membrane. A conclusion from these results is that a catalyst with lower coke tendency is needed to apply this combination of Pd membrane and TZFBR.
机译:描述了钯中空纤维膜与两区流化床反应器(TZFBR)的组合用于丙烷的催化脱氢。该配置旨在将TZFBR提供的原位催化剂再生与Pd膜可实现的转化率提高相结合,Pd膜可从反应器中除去氢气,从而提高了反应速率,理论上讲其转化率甚至高于平衡转化率。实验表明,Pd中空纤维膜可有效地从反应介质中除去氢,并且使用Pt-Sn / Al2O3催化剂,尽管催化剂的焦化增加,TZFBR仍可实现稳态运行。然而,使用这种催化剂,由氢的去除引起的更快的焦炭形成超过了氢的去除的有益效果,并且在膜的存在下,给定进料可达到的产率较低。从这些结果得出的结论是,需要较低焦炭趋势的催化剂来应用Pd膜和TZFBR的这种组合。

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