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The modeling of oxygen transport in MIEC oxide hollow fiber membranes

机译:MiC氧化中空纤维膜中氧气输送的建模

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摘要

The paper presents a model of oxygen transport in oxygen-permeable hollow fiber membranes taking into account the gradual changes of oxygen partial pressure in flows of feed and sweep gases along the HF membrane. The model is based on fulfilling local mass balance conditions linking oxygen flows in feed and sweep gases with the oxygen flux through the membrane. Computer simulation of oxygen permeation data for hollow fiber membranes made from mixed ionic electronic conducting oxides (Ba0.5Sr0.5Co0.8Fe0.2O3-delta, Ba0.5Sr0.5Co0.78W0.02Fe0.2O3-delta and Ba0.5Sr0.5Co0.75Mo0.05Fe0.2O3-delta) was carried out using different models. The oxygen permeability model based on the semi-empirical dependence of the oxygen flux on oxygen partial pressure J(O2) = gamma(T)(pO(2,1)(n) - pO(2,2)(n)) gives the most accurate description of the experimental data. An analysis of the activation energy of the effective oxygen flux coefficient gamma(T) indicates that the rate determining step is a surface reaction.
机译:本文介绍了透氧中空纤维膜中的氧气输送模型,考虑了沿HF膜饲料流动流和扫气流中的氧分压的逐渐变化。该模型基于满足局部质量平衡条件,将氧气流入进料和扫气液中的氧气通量通过膜。计算机仿真氧气渗透数据用于由混合离子电子导电氧化物制成的中空纤维膜(BA0.5SR0.5CO0.8FE0.2O3-DELTA,BA0.5SR0.5CO0.78W0.02FE0.2O3-DELTA和BA0.5SR0.5CO0。使用不同的型号进行75mo0.05fe0.2o3-delta)。基于氧气通量对氧分压J(O2)=γ(T)(PO(2,1) - PO(2,2)(n))的氧气渗透性模型给予实验数据的最准确描述。对有效氧气磁通系数γ(T)的活化能量的分析表明速率确定步骤是表面反应。

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