论文标题
由催化表面上的扩散流动流动驱动的不稳定性
Instabilities driven by diffusio-phoretic flow on catalytic surfaces
论文作者
论文摘要
我们从理论和数值上研究由沿反应表面的溶质浓度梯度引起的扩散流动流动的不稳定性。重要的控制参数是Peclet数字PE,它量化了溶质对流率与扩散率的比率。首先,我们研究了二维催化平面上的弥散性流动流。从线性稳定性分析中,我们可以获得大于8pi的PE,对流的大众传输超过了通过扩散的,并且会产生对称性的模式,这与数值结果一致。对于更大的PE,非线性术语变得很重要。对于大于16pi的PE,从催化平面发出了多个浓度羽流,最终将其合并为一个较大的羽流。当PE更大时,会有连续的排放和浓度羽流的事件。这种新发现的流状态反映了系统的非线性饱和度。向该状态的过渡的关键小子数取决于Schmidt号码SC。在本文的第二部分中,我们对球形催化颗粒进行了三维模拟,而超越关键的小子数再次发现了连续的羽状发射和羽状合并,现在导致了裂纹粒子的混乱运动。因此,我们的结果有助于了解高PE机制中催化颗粒的实验观察到的混乱运动。
We theoretically and numerically investigate the instabilities driven by diffusiophoretic flow, caused by a solutal concentration gradient along a reacting surface. The important control parameter is the Peclet number Pe, which quantifies the ratio of the solutal advection rate to the diffusion rate. First, we study the diffusiophoretic flow on a catalytic plane in two dimensions. From a linear stability analysis, we obtain that for Pe larger than 8pi, mass transport by convection overtakes that by diffusion, and a symmetry-breaking mode arises, which is consistent with numerical results. For even larger Pe, non-linear terms become important. For Pe larger than 16pi, multiple concentration plumes are emitted from the catalytic plane, which eventually merges into a single larger one. When Pe is even larger, there are continuous emissions and merging events of the concentration plumes. This newly-found flow state reflects the non-linear saturation of the system. The critical Peclet number for the transition to this state depends on Schmidt number Sc. In the second part of the paper, we conduct three-dimensional simulations for spherical catalytic particles, and beyond a critical Peclet number again find continuous plume emission and plume merging, now leading to chaotic motion of the phoretic particle. Our results thus help to understand the experimentally observed chaotic motion of catalytic particles in the high Pe regime.