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Preparation and Characterization of Dual-Layer Hollow Fibre Catalyst Membrane for Oxygen Transport

机译:双层中空纤维催化剂膜的制备与表征氧气运输

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Asymmetric pore configuration of dual-layer hollow fibre catalyst membrane of NiO-YSZ (inner layer)/La_(0.7)Sr_(0.3)Co_(0.2)Fe_(0.8)O_(3-δ)-YSZ (outer layer) has been studied from its morphology and oxygen transport point of view. The membrane was synthesized by phase inversion method and co-extruded using water as the external coagulant and water, ethanol and NMP mixture as the internal coagulant (bore liquid mixture), followed by sintering at 1300 °C for 8h. Volume ratio of water: ethanol:NMP was 4:1:5. The resulted dual-layer membrane has non-sandwich like pore configuration. SEM images of the membrane showed finger-like pores on the internal side and sponge-like pores on the external side. Bending strength of the membrane was 9.76 MPa and nitrogen permeability (gas tightness) was 1.36 × 10~(-4) mol.m~(-2).s~(-2).Pa~(-1). The oxygen permeability of the membrane at 600, 700 and 800 °C was 2.78 × 10~(-8), 2.84 × 10~(-8) and 3.10 × 10~(-8) mol.s~(-1) .cm~(-2), respectively, which is about two order of magnitude lower than oxygen permeability of other reported perovskite-based membranes.
机译:Nio-YSZ(内层)/ LA_(0.7)SR_(0.3)CO_(0.2)FE_(0.8)O_(3-Δ)-ysz(外层)的双层中空纤维催化剂膜的不对称孔径构型。已经存在从其形态学和氧气传输的角度研究。通过相转化方法合成膜,并使用水作为内部凝结剂和水,乙醇和NMP混合物共挤出,作为内部凝结剂(孔液混合物),然后在1300℃下烧结8小时。水的体积比:乙醇:NMP为4:1:5。得到的双层膜具有非夹心构型。膜的SEM图像显示在内侧的手指状毛孔,外侧的海绵状孔。膜的弯曲强度为9.76MPa和氮气渗透率(气体密封)为1.36×10〜(-4)Mol.m〜(-2)。 - PA〜(-1)。膜在600,700和800℃下的氧气渗透率为2.78×10〜(-8),2.84×10〜(-8)和3.10×10〜(-8)摩尔〜(-1)。 Cm〜(-2)分别是比其他报告的钙钛矿的膜的透氧率低约两个数量级。

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