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Modeling of a SrCe_(0.95)Yb_(0.05)O_(3-α) Hollow Fibre Membrane Reactor for Methane Coupling

机译:甲烷偶联用SrCe_(0.95)Yb_(0.05)O_(3-α)中空纤维膜反应器的建模

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摘要

Proton-hole mixed conductor, SrCe_(0.95)Yb_(0.05)O_(3-α)(SCYb), has the potential to be used as a membrane for dehydrogenation reactions such as methane coupling due to its high C_2-selectivity and its simplicity for fabricating reactor systems. In addition, the mixed conducting membrane in the hollow fibre geometry is capable of providing high surface area per unit volume. In this study, mechanism of methane coupling reaction on the SCYb membrane was proposed and the kinetic parameters were obtained by regression of experimental data. A mathematical model describing the methane coupling in the SCYb hollow fibre membrane reactor was also developed. With this mathematical model, various operating conditions such as the operation mode, operation pressure and feed concentrations affecting performance of the reactor were investigated. The simulation results show that the cocurrent flow in the reactor exhibits higher conversion of methane and higher yield of ethylene compared to the countercurrent flow. In order to achieve the highest C_2 yield, especially of ethylene, pure methane should be used as feed and the operating pressure be 300 kPa. Air can be used as the source of oxygen for the reaction and its optimum feed velocity is twice of the methane feed velocity. The air pressure in the lumen side should be kept the same as or slightly lower than the pressure of shell side.
机译:质子孔混合导体SrCe_(0.95)Yb_(0.05)O_(3-α)(SCYb)由于具有高的C_2选择性和简单性,因此有潜力用作甲烷偶联等脱氢反应的膜。用于制造反应器系统。另外,中空纤维几何形状的混合导电膜能够提供每单位体积高的表面积。提出了SCYb膜上甲烷偶联反应的机理,并通过实验数据的回归获得了动力学参数。还建立了描述SCYb中空纤维膜反应器中甲烷偶联的数学模型。利用该数学模型,研究了各种操作条件,例如操作模式,操作压力和进料浓度对反应器性能的影响。模拟结果表明,与逆流相比,反应器中的并流显示出更高的甲烷转化率和更高的乙烯收率。为了获得最高的C_2收率,尤其是乙烯的C_2收率,应使用纯甲烷作为进料,操作压力为300 kPa。空气可用作反应的氧气源,其最佳进料速度是甲烷进料速度的两倍。管腔侧的气压应保持与壳侧的气压相同或略低。

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