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Analysis and modeling of hydrogen permeation through alumina membranes with finely dispersed palladium

机译:细分散钯穿过氧化铝膜的氢渗透分析和建模

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The alpha-alumina disk with 0.85 mu m-thickness finely dispersed palladium was prepared by spin dipping. The fluxes of pure hydrogen and nitrogen through this membrane were measured at temperatures of 423-573 K and pressures difference up to 225 kPa. In the case of the pressure difference of 80 kPa, the ideal separation factor of H-2/N-2 increased from 3.4 at 423 K to 4.4 at 573 K. Furthermore, the effects of operating temperature and pressure on the transport behaviors of hydrogen through the membrane were analyzed based on the resistance model. The results demonstrated that the hydrogen permeation through this membrane was categorized into two regimes. About 41-58% of hydrogen flux was contributed by Knudsen diffusion in the temperature range of 423-473 K. Within the temperature ranging from 523 K to 573 K, the hydrogen permeance increased with increasing temperature. This is about 52-73% of the overall permeance and is attributed to the solution-diffusion mechanism in this regime. [References: 22]
机译:通过旋转浸渍制备具有0.85μm厚度的精细分散的钯的α-氧化铝盘。在423-573 K的温度和高达225 kPa的压差下测量了通过该膜的纯氢气和氮气的通量。在压力差为80 kPa的情况下,H-2 / N-2的理想分离系数从423 K时的3.4增加到573 K时的4.4。此外,操作温度和压力对氢的传输行为的影响通过膜的阻力模型进行了分析。结果表明,通过该膜的氢渗透分为两种方案。在423-473 K的温度范围内,克努德森扩散贡献了约41-58%的氢通量。在523 K至573 K的温度范围内,氢的渗透率随温度的升高而增加。这约占总渗透率的52-73%,并归因于该方案中的溶液扩散机制。 [参考:22]

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