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Partial Oxidation of Methane on a Nickel Catalyst: Kinetic Monte-Carlo Simulation Study

机译:镍催化剂上甲烷的部分氧化:动力学monte-Carlo   模拟研究

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摘要

Kinetic Monte-Carlo simulation is applied to study the partial oxidation ofmethane over a nickel catalyst. Based on the Langmuir-Hinshelwood mechanism,the kinetic behavior of this reaction is analyzed and the results are comparedwith previous experiments. This system exhibits kinetic phase transitionsbetween reactive regions with sustained reaction and poisoned regions withoutreaction. The fractional coverages of the adsorbed species and the productionrates of H2, CO, H2O, and CO2 are evaluated at steady state as functions offeed concentration of the methane and oxygen, and reaction temperature. Theinfluence of lattice coordination number, diffusion, and impurities on thesurface is investigated. The simulation results are in good agreement with theexperimental studies where such results are available. It is observed that whenthe lattice coordination number is increased to eight, the width of thereactive region increases significantly. Moreover, the phase transition becomescontinuous. The diffusion of adsorbed O and H on the surface plays a measurablerole in the reaction, increasing the maximum production rates as the diffusionrate increases. In systems with impurities, the production rates are greatlyreduced and the phase transition is also changed from being abrupt tocontinuous.
机译:动力学蒙特卡洛模拟用于研究镍催化剂上甲烷的部分氧化。基于Langmuir-Hinshelwood机理,分析了该反应的动力学行为,并将结果与​​以前的实验进行了比较。该系统在具有持续反应的反应区域和没有反应的中毒区域之间显示出动力学相变。在稳态下,根据甲烷和氧气的进料浓度和反应温度来评估吸附物质的分数覆盖率以及H2,CO,H2O和CO2的生产率。研究了晶格配位数,扩散和杂质对表面的影响。仿真结果与可获得此类结果的实验​​研究非常吻合。观察到,当晶格配位数增加到八个时,反应区的宽度显着增加。而且,相变变得连续。吸附的O和H在表面上的扩散在反应中起可测量的作用,随着扩散率的增加,最大生产率提高。在具有杂质的系统中,生产率大大降低,并且相变也从突变变为连续。

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