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Numerical investigation of oxygen permeation and methane oxy-combustion in a stagnation flow ion transport membrane reactor

机译:滞流离子迁移膜反应器中氧渗透和甲烷氧燃烧的数值研究

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摘要

In this work, a two-step oxy-combustion reaction kinetics model for methane-oxygen combustion is used to predict the oxy-combustion characteristics in the permeate side of the membrane. More accurate permeation rate characteristics inside this simple symmetric design ITM reactor is also expected using this model. New oxygen permeation model is introduced in this work for an LSCF-1991 ion transport membrane. The simulation of the oxygen permeation process across the membrane has been performed through series of visual C++ user defined function compiled and incorporated to FLUENT. The analysis of the permeation process has been conducted for separation only process (no reactions) using an inert gas (argon) as a sweep gas and a comparison has been done with cases of using CH_4 plus CO_2 as sweep gases. The effect of reactivity using the same sweep gases (CH_4 plus CO_2) is investigated by comparing the same cases with and without reactions in the permeate side. It was found that there are important parameters affecting the operation of ITM reactors like the inlet gases temperature, percentage of CH_4 in the sweep gases mixture and the reactor geometry. Also, there are less important parameters like, feed and sweep volume flow rates, oxygen partial pressure in the feed side.
机译:在这项工作中,使用用于甲烷-氧气燃烧的两步氧气燃烧反应动力学模型来预测膜渗透侧的氧气燃烧特性。使用此模型,也有望在此简单的对称设计ITM反应器中获得更准确的渗透速率特性。在这项工作中,针对LSCF-1991离子迁移膜引入了新的氧气渗透模型。通过一系列可视化的C ++用户定义函数进行了模拟,该过程跨膜进行了氧气渗透过程的模拟,该函数已编译并合并到FLUENT中。已经使用惰性气体(氩气)作为吹扫气对仅分离过程(无反应)进行了渗透过程的分析,并且与使用CH_4加CO_2作为吹扫气的情况进行了比较。通过比较渗透物侧有反应和无反应的相同情况,研究了使用相同吹扫气体(CH_4加CO_2)的反应性影响。发现存在影响ITM反应器运行的重要参数,例如入口气体温度,吹扫气体混合物中CH_4的百分比以及反应器的几何形状。此外,还有一些不太重要的参数,例如进料和吹扫体积流速,进料侧的氧气分压。

著录项

  • 来源
    《Energy》 |2013年第6期|322-332|共11页
  • 作者单位

    KACST-TIC for CCS, Mechanical Engineering Department, Faculty of Engineering, KFUPM, Dhahran 31261, Saudi Arabia;

    KACST-TIC for CCS, Mechanical Engineering Department, Faculty of Engineering, KFUPM, Dhahran 31261, Saudi Arabia, Mechanical Engineering Department, Alexandria University, Egypt;

    KACST-TIC for CCS, Mechanical Engineering Department, Faculty of Engineering, KFUPM, Dhahran 31261, Saudi Arabia;

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  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Ion transport membrane; Membrane reactor; Reactions kinetics; Permeation process;

    机译:离子传输膜膜反应器反应动力学;渗透过程;

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