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Upscaling Mass Transport with Homogeneous and Heterogeneous Reaction in Porous Media

机译:多孔介质中均相和非均相反应的大规模传质

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The upscaling process of mass transport with chemical reaction in porous media isrncarried out using the method of volume averaging under diffusive and dispersivernconditions. We study cases in which the (first-order) reaction takes place in the fluidrnphase that saturates the porous medium or when the reaction occurs at the solid-fluidrninterface. The upscaling effort leads to average transport equations, which are expressedrnin terms of effective medium coefficients for (diffusive or dispersive) mass transportrnand reaction that are computed by solving the associated closure problems inrnrepresentative unit cells. Our derivations show that mass transport effective coefficientsrndepend, in general, of the nature and magnitude of the microscopic reaction raterncoefficient as well as of the essential geometrical structure of the solid matrix and thernflow rate. Furthermore, if the chemical reaction is homogeneous, the effective reactionrnrate coefficient is found to be simply the multiplication of its microscopic counterpartrnwith the porosity; whereas, if the reaction is heterogeneous, the effective reactionrncoefficient is determined from a closure problem solution.
机译:在扩散和分散条件下,采用体积平均法进行了在多孔介质中具有化学反应的传质放大过程。我们研究了其中(一阶)反应发生在使多孔介质饱和的流体相中或当反应发生在固液界面时的情况。扩大工作量导致了平均输运方程,该方程以有效的介质系数(扩散或分散)和反应的有效介质系数表示,该系数是通过解决代表性单位晶胞的相关封闭问题而计算出的。我们的推导表明,传质有效系数通常取决于微观反应速率系数的性质和大小,以及固体基质的基本几何结构和流量。此外,如果化学反应是均匀的,则发现有效反应速率系数只是其微观对应物与孔隙率的乘积。反之,如果反应是非均质的,则根据封闭问题解来确定有效的反应系数。

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