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Sulfuric acid-modified zirconia membrane for use in hydrogen separation

机译:用于氢分离的硫酸改性氧化锆膜

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Microporous zirconia membranes, in which the pore size distribution was controlled by optimizing the calcination temperature, were prepared by a sol-gel technique. The membrane with an average pore size < 2 nm was then modified by exposure to sulfuric acid (H_2SO_4) solutions, followed by heat-treatment. The gas permeation properties of the membranes were evaluated for single-component and binary-component systems of H_2, N_2, CO_2, iso-C_4H_(10) and NH_3. The zirconia membrane, which was modified by treatment with a 0.50 mol l~(-1) H_2SO_4 solution, showed a high hydrogen permeance of (2.8-3.0) x 10~(-6) mol Pa~(-1) m~(-2) s~(-1), and the H_2 selectivities over CO_2 and iso-C_4H_(10) were 6 and 9, respectively, for equimolar binary systems. The experimental data showed that the H_2 selectivity over the other gases increased, and the permeance devreased, when increasing concentration of the H_2SO_4 solution were used. The permeance of NH_3 for the H_2SO_4-modified membranes suggests that acidic sites were introduced as a result of the modification.
机译:通过溶胶-凝胶技术制备了微孔氧化锆膜,其中通过优化煅烧温度来控制孔径分布。然后通过暴露于硫酸(H_2SO_4)溶液,对平均孔径<2 nm的膜进行修饰,然后进行热处理。对于H_2,N_2,CO_2,iso-C_4H_(10)和NH_3的单组分和二组分体系,评估了膜的气体渗透性能。经0.50 mol l〜(-1)H_2SO_4溶液改性的氧化锆膜表现出较高的氢渗透率(2.8-3.0)x 10〜(-6)mol Pa〜(-1)m〜( -2)s〜(-1),对于等摩尔二元体系,CO_2和iso-C_4H_(10)的H_2选择性分别为6和9。实验数据表明,当使用浓度较高的H_2SO_4溶液时,对其他气体的H_2选择性增加,渗透率降低。 NH_3对H_2SO_4修饰的膜的渗透性表明,酸性位点是由于修饰而引入的。

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