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Influence of buoyancy-driven convection on the dynamics of A plus B -> C reaction fronts in horizontal solution layers

机译:浮力驱动的对流对水平溶液层中A + B-> C反应前沿动力学的影响

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The dynamics of initially vertical A+B -> C reaction fronts propagating in covered horizontal solution layers can be influenced by buoyancy-driven convection. Experiments have provided evidence that a much faster propagation of the front occurs in solutions than that predicted by reaction-diffusion (RD) theories, thereby suggesting the influence of convective effects arising if A, B, and C have different densities. Here we analyze numerically and theoretically the dynamics resulting from the coupling of a simple A+B -> C chemical reaction with diffusion and convection induced by density differences across the reaction front. The important parameters of the related reaction-diffusion-convection (RDC) model are the three dimensionless Rayleigh numbers, quantifying the contribution of each species concentration to the density of the solution, the layer thickness, and the initial reactant concentration ratio. The presence of buoyancy-driven convection at the front induces a propagation of this front even in the case of equal diffusion coefficients and equal initial reactant concentrations for which RD theories predict a non-moving front. In the case of equal initial concentrations, even in the presence of convection, the classification of the various possible dynamics and the prediction of the direction of front propagation can be obtained from simple criteria on the Rayleigh numbers. In the case of different initial reactant concentrations for which, in the absence of convection, the RD front propagates towards the side of the less concentrated reactant, the introduction of buoyancy convection not only invalidates the long time RD scalings but can lead to a double reversal in the direction of propagation of the reaction front for intermediate times. The influence of the different parameters on the RDC dynamics is presented.
机译:浮力驱动的对流会影响在覆盖的水平溶液层中传播的初始垂直A + B-> C反应前沿的动力学。实验提供的证据表明,溶液中前沿发生的扩散要比反应扩散(RD)理论所预测的快得多,从而表明如果A,B和C的密度不同,则对流效应的影响。在这里,我们在数值和理论上分析由简单的A + B-> C化学反应与整个反应前沿的密度差异引起的扩散和对流耦合所产生的动力学。相关的反应扩散对流(RDC)模型的重要参数是三个无量纲瑞利数,用于量化每种物质浓度对溶液密度,层厚度和初始反应物浓度比的贡献。即使在相同的扩散系数和相等的初始反应物浓度的情况下,浮力驱动的对流在前缘处也会引起该前缘的传播,而RD理论为此预测了不移动的前缘。在相等的初始浓度的情况下,即使存在对流,也可以从关于瑞利数的简单标准中获得各种可能的动力学的分类以及对前传播方向的预测。在不同的初始反应物浓度的情况下,在没有对流的情况下,RD前沿向浓度较低的反应物一侧传播,浮力对流的引入不仅使长时间的RD结垢无效,而且可能导致双重逆转在反应前沿传播方向上的中间时间。提出了不同参数对RDC动力学的影响。

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