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Modeling of U-shaped Ba0.5Sr0.5Co0.8Fe0.2O3-δ hollow-fiber membrane for oxygen permeation

机译:U型Ba0.5Sr0.5Co0.8Fe0.2O3-δ中空纤维膜透氧模型

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摘要

A mathematic model is developed for the perovskite-type mixed ionic-electronic conducting (MIEC) membrane,which makes it possible to simulate the process of oxygen separation in the U-shaped Ba0.5Sr0.5Co0.8Fe0.2O3-δ hollow-fiber membrane.The model correlates the oxygen permeation flux to the measurable variables.The trends of calculated results for purge operation coincide well with the experimental data,therefore the model is considerable for flux prediction under vacuum operation.Higher oxygen separation efficiency can be achieved with vacuum operation than purge operation.Parameter study with vacuum operation reveals that oxygen permeation flux increases with higher vacuum levels,and vacuum pressure of around 1.013 × 103 Pa is the optimal.Also,vacuum operation on the lumen side is much more efficient to achieve higher oxygen permeation flux compared with compression mode on the shell side.
机译:建立了钙钛矿型混合离子电导(MIEC)膜的数学模型,从而可以模拟U型Ba0.5Sr0.5Co0.8Fe0.2O3-δ中空纤维中氧的分离过程。该模型将氧气渗透通量与可测量变量相关联。吹扫操作的计算结果趋势与实验数据吻合良好,因此该模型对于真空操作下的通量预测具有重要意义。真空可以实现更高的氧气分离效率真空操作的参数研究表明,真空度越高,氧气的渗透通量就越大,并且真空压力约为1.013×103 Pa是最佳的。此外,管腔侧的真空操作更有效地获得更高的氧气。渗透通量与壳侧压缩模式相比。

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  • 来源
    《中国化学工程学报(英文版)》 |2017年第7期|892-897|共6页
  • 作者单位

    School of Chemistry and Chemical Engineering, South China University of Technology, Guangzhou 510640, China;

    School of Chemistry and Chemical Engineering, South China University of Technology, Guangzhou 510640, China;

    School of Chemistry and Chemical Engineering, South China University of Technology, Guangzhou 510640, China;

  • 收录信息 中国科学引文数据库(CSCD);中国科技论文与引文数据库(CSTPCD);
  • 原文格式 PDF
  • 正文语种 eng
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