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Hydrogen separation from blended natural gas and hydrogen by Pd-based membranes

机译:钯基膜从混合天然气和氢气中分离氢

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Hydrogen separation membranes based on a heated metal foil of a palladium alloy, offer excellent permeability for hydrogen as a result of the solution-diffusion mechanism. Here, the possibility to separate hydrogen from the mixture of Natural Gas (NG) and hydrogen (NG+H-2) with various NG concentrations using Pd, PdCu53 and PdAg24 hydrogen purification membranes is demonstrated. Hydrogen concentrations above similar to 25% (for Pd and PdCu53) and similar to 15% (for PdAg24) were required for the hydrogen separation to proceed at 400 degrees C and 5 bar pressure differential. Hydrogen permeability of the studied alloys could be almost fully recovered after switching the feed gas to pure hydrogen, indicating no significant interaction between the natural gas components and the membranes surface at the current experimental condition. Hydrogen flux of the membranes at various pressure differential was measured and no changes in the hydrogen permeation mechanism could be noticed under (NG 50%+H-2) mixture. The hydrogen separation capability of the membranes is suggested to be mainly controlled by the operating temperature and the hydrogen partial pressure. (C) 2019 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:基于溶液扩散机制,基于钯合金加热金属箔的氢分离膜可提供出色的氢渗透性。在此,展示了使用Pd,PdCu53和PdAg24氢纯化膜从天然气(NG)和氢气(NG + H-2)的混合物中分离出氢气的可能性。要在400摄氏度和5 bar压差下进行氢分离,需要高于25%(对于Pd和PdCu53)和接近15%(对于PdAg24)的氢浓度。将原料气转换为纯氢后,所研究合金的氢渗透性几乎可以完全恢复,这表明在当前实验条件下,天然气组分与膜表面之间没有明显的相互作用。在(NG 50%+ H-2)混合物下,测量了膜在不同压差下的氢通量,并且没有观察到氢渗透机理的变化。建议膜的氢分离能力主要由操作温度和氢分压控制。 (C)2019氢能出版物有限公司。由Elsevier Ltd.出版。保留所有权利。

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