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Modeling of termokinetic oscillations at partial oxidation of methane

机译:甲烷部分氧化下术语振动的建模

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Partial oxidation of natural gas at moderate temperatures below 1500 K has significant interest for a number of industrial applications. But such processes can proceed at different unstable regimes including oscillating modes. Nonlinear phenomena at partial oxidation of methane were observed at different conditions. The investigation of the complex nonlinear system of equations that describes this process is a real method to insure its stability at industrial conditions and, at the same time, is an effective tool for its further enhancement. Numerical analysis of methane oxidation kinetics in the continuous stirred-tank reactor, with the use of detailed kinetic model has shown the possibility of the appearance of oscillating modes in the appropriate range of reaction parameters that characterize the composition, pressure, reagents flow, thermophysical features of the system, and geometry of the reactor. The appearance of oscillating modes is connected both with the reaction kinetics, heat release and sink and reagents introduction and removing. At that, oscillations appear only at a limited range of parameters, but can be accompanied by significant change in the yield of products. We have determined the range of initial temperature and pressure at which oscillations can be observed, if all other parameters remained fixed. The boundaries of existence of oscillations on the phase plane were calculated. It was shown that depending on the position inside the oscillation region the oscillations have different frequency and amplitude. It was reviled the role of heat exchange with the environment: at the absence of heat exchange the oscillating modes are impossible. In the vicinity of the boundary of phase range, where oscillations exist, significant change of concentration of some products were observed, for example, that of CO_2, which in this case one of the principal products is. At that, insignificant increase in pressure not only change the character of CO_2 behaving with time, but as well lead to significant increase of its mole fraction simultaneously twice decreasing the mole fraction of CO.
机译:在低于1500ķ气温适中天然气的部分氧化有许多工业应用的显著利益。但是,这种方法可以在不同的不稳定的政权,包括振荡模式进行。在不同条件下观察到在甲烷部分氧化非线性现象。描述此过程方程的复杂的非线性系统的调查是在工业条件下,以确保其稳定的真正方法,并且在同一时间,为它的进一步增强的有效工具。在连续搅拌釜反应器中的甲烷氧化动力学,与使用的详细的动力学模型的数值分析已经显示出表征组成,压力反应参数,试剂流动,热物理特征的适当范围的振荡模式的外观的可能性该系统中,并且将反应器的几何形状。振荡模式的外观与反应动力学,热释放和水槽和试剂引入和去除连接两者。在那个,振荡仅在参数的有限范围出现,但可以通过在产品的产量显著变化陪同。我们已经确定在该振荡可以观察到初始温度和压力的范围内,如果所有其它参数保持固定。在相平面上振荡的存在的边界进行了计算。结果表明,根据振动区域内的位置的振荡具有不同的频率和幅度。有人唾骂与环境的热交换的作用:在没有热交换的振荡模式是不可能的。在相位范围,其中存在的振荡的边界附近时,观察到一些产物的浓度的变化显著,例如,CO_2,在这种情况下,主要的产品之一是的。在那个,微不足道的压力增加不仅改变CO_2运行得的字符与时间,但也导致其摩尔分数同时两次降低CO的摩尔分数的显著增加。

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