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Application of palladium membrane reactor for dehydrogenation of propane

机译:钯膜反应器在丙烷脱氢中的应用

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The dehydrogenation of propane in palladium membrane reactors was simulated using two models, i.e. the plug flow and radial diffusion models. The expression of hydrogen permeation through a Pd-Ag membrane was obtained from experiments at 673,773 and 873 K, assuming that the permeation follows Sievert's law. The simulation results agreed well with the experimental values in the membrane reactor for the dehydrogenation of propane on Pt-Sn-K/gamma -Al2O3. The membrane thickness played an important role in the performance of the membrane reactor. The conversion of propane was independent of the N-2 Sweep flow rate when the membrane thickness was larger than 100 mum. Conversely, when the membrane thickness decreased, the conversion increased and gradually leveled off. The effect of radial diffusion was significant at a membrane thickness of 10 mum. [References: 13]
机译:使用两种模型,即活塞流和径向扩散模型,模拟了钯膜反应器中丙烷的脱氢。通过Pd-Ag膜渗透氢的表达是从673,773和873 K的实验中获得的,假设渗透遵循西弗特定律。模拟结果与在Pt-Sn-K /γ-Al2O3上丙烷脱氢的膜反应器中的实验值非常吻合。膜厚度在膜反应器的性能中起重要作用。当膜厚度大于100微米时,丙烷的转化率与N-2吹扫流速无关。相反,当膜厚度减小时,转化率增加并逐渐趋于平稳。径向扩散的影响在10微米的膜厚度下很明显。 [参考:13]

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