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Prediction of CO_2/H_2 Separation Properties of NaY Zeolite Membranes under Multicomponent Mixture Conditions

机译:多组分混合条件下NaY沸石膜的CO_2 / H_2分离性能预测

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The separation performances of a NaY-type zeolite membranes- -were evaluated in terms of permeance and selectivity as a function of temperature and-feed pressure by coupling a modified Knudsen mechanism with the surface diffusion with a multicomponent approach. After model validation in a-wide temperature range (0-400°C) using slngle-gas experimental data from the literature [2-3], the model was applied to predict the permeation performances in binary mixture conditions, which showed a permeation,behaviour quite different from the single-gas case. As the main result, CO_2 and H_2 permeation trends with temperature are found to be different from each other, with the former being decreasing and the latter increasing/with it This results in a selectivity decreasing with temperature,-forecasting that adopting temperature below 0°C at the/low pressure values considered could importantly -enhance the CO_2/H_2 separation efficiency thanks to the|Stronger blocking effect caused by CO_2 towards the H_2 permeation. Furthermore, the feed pressure is found to decrease/the permeance of both CO_2 and H_2, whereas their selectivity remains basically constant in the feed pressure range of 400-1000 kPa.
机译:通过将改良的努森机制与表面扩散与多组分方法结合,根据渗透率和选择性作为温度和进料压力的函数,评估了NaY型沸石膜的分离性能。在使用文献[2-3]的单气体实验数据在一个宽温度范围(0-400°C)内对模型进行验证之后,该模型可用于预测在二元混合条件下的渗透性能,表明其渗透性,行为与单气体情况大不相同。作为主要结果,发现CO_2和H_2随温度的渗透趋势彼此不同,前者降低,而后者升高/随温度升高。这导致选择性随温度降低,这是因为预测采用0°C以下的温度由于CO_2对H_2的渗透产生更强的阻断作用,在所考虑的/低压值下的C可以重要地提高CO_2 / H_2的分离效率。此外,发现进料压力降低/ CO_2和H_2两者的渗透/渗透,而它们的选择性在400-1000kPa的进料压力范围内基本保持恒定。

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