Laboratoire Fluides Automatique et Systèmes Thermiques, Universités P. et M. Curie and Paris Sud, C.N.R.S. (UMR7608), Bâtiment 502, Campus Universitaire, 91405 Orsay Cedex, France.
Chaos. 2012 Sep;22(3):037108. doi: 10.1063/1.4734489.
Autocatalytic reaction fronts between two reacting species in the absence of fluid flow, propagate as solitary waves. The coupling between autocatalytic reaction front and forced simple hydrodynamic flows leads to stationary fronts whose velocity and shape depend on the underlying flow field. We address the issue of the chemico-hydrodynamic coupling between forced advection in porous media and self-sustained chemical waves. Towards that purpose, we perform experiments over a wide range of flow velocities with the well characterized iodate arsenious acid and chlorite-tetrathionate autocatalytic reactions in transparent packed beads porous media. The characteristics of these porous media such as their porosity, tortuosity, and hydrodynamics dispersion are determined. In a pack of beads, the characteristic pore size and the velocity field correlation length are of the order of the bead size. In order to address these two length scales separately, we perform lattice Boltzmann numerical simulations in a stochastic porous medium, which takes into account the log-normal permeability distribution and the spatial correlation of the permeability field. In both experiments and numerical simulations, we observe stationary fronts propagating at a constant velocity with an almost constant front width. Experiments without flow in packed bead porous media with different bead sizes show that the front propagation depends on the tortuous nature of diffusion in the pore space. We observe microscopic effects when the pores are of the size of the chemical front width. We address both supportive co-current and adverse flows with respect to the direction of propagation of the chemical reaction. For supportive flows, experiments and simulations allow observation of two flow regimes. For adverse flow, we observe upstream and downstream front motion as well as static front behaviors over a wide range of flow rates. In order to understand better these observed static state fronts, flow experiments around a single obstacle were used to delineate the range of steady state behavior. A model using the "eikonal thin front limit" explains the observed steady states.
在没有流体流动的情况下,两种反应物质之间的自动催化反应前沿以孤立波的形式传播。自动催化反应前沿与强制单相流体流动的耦合会导致固定前沿,其速度和形状取决于基础流场。我们研究了强制平流在多孔介质中与自维持化学波之间的化学-水动力耦合问题。为此,我们在透明填充珠多孔介质中进行了广泛的流速实验,包括碘酸亚砷酸和亚氯酸盐-四硫代硫酸盐自催化反应。这些多孔介质的特性,如它们的孔隙率、曲折度和水动力弥散度都得到了确定。在填充珠中,特征孔径和速度场相关长度与珠的大小相当。为了分别处理这两个长度尺度,我们在随机多孔介质中进行了格子玻尔兹曼数值模拟,该模拟考虑了对数正态渗透率分布和渗透率场的空间相关性。在实验和数值模拟中,我们观察到以几乎恒定的前沿宽度恒定速度传播的固定前沿。在具有不同珠大小的填充珠多孔介质中没有流动的实验表明,前沿传播取决于扩散在孔隙空间中的曲折性质。当孔隙尺寸与化学前沿宽度相当时,我们观察到微观效应。我们研究了与化学反应传播方向一致和相反的支持共流和不利流动。对于支持流,实验和模拟允许观察到两种流动状态。对于不利流动,我们观察到上游和下游前沿运动以及在广泛的流速范围内的静态前沿行为。为了更好地理解这些观察到的静态前沿,我们使用单个障碍物周围的流动实验来描绘稳态行为的范围。使用“尖峰薄前沿极限”的模型解释了观察到的稳态。