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Darcy and post-Darcy flows within different sands

机译:达西和达西后流在不同的沙子中流动

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The subject of non-Darcy flow spans many engineering disciplines. The Authors have presented the results of interesting research on flow through a fine porous media in which high Reynolds numbers were induced. A number of issues can be raised: (ⅰ) In their Abstract the Authors make the rather definitive assertion that non-Darcy flow begins at a Reynolds number of 4.3, and present Fig. 7 to support this claim. In fact, in the section before "Conclusion" on p. 524, the Authors show that the value of 4.3 arises from the arbitrary selection of 0.95 for the ratio of viscosity-induced friction to total friction. They also show that a ratio of 0.99 yields Re = 0.93, instead of Re = 4.3. This is consistent with the fact that it has long been recognized that there is no single value of Re at which it can be said that Darcy's Law breaks down. In this respect the nature of the transition from linear to post-linear flow shown in Fig. 7 is no different than many other such plots that have appeared in the literature, and supports the communis opinio that the transition is gradual. Examples of similar plots can be found in the following references: Rose (1945a,b), Ergun (1952), Arbhabhirama and Dinoy (1973)—a family of curves, McCorquodale et al. (1978)—large unified data-set, and Fand and Thinakaran (1990)—expanding the work of Reichelt (to name just a few). Although these various references often show more scatter about their fitted curves than does the author's Fig. 7, they all show a gradual transition from a linear to a non-linear relationship, regardless of how the friction factor and Reynolds number terms are defined. In fact, even though flow through pipes does go through a well-known and sudden transition (from laminar flow to partially developed turbulent flow), the commonly stated figure of Re = 2000 is also known to be an approximate value. The assertion in the abstract that non-Darcy flow through porous media begins at a Reynolds number of 4.3, made again in the section entitled "Conclusion", is therefore not justified.
机译:非达西流的主题涉及许多工程学科。作者已经提出了有趣的研究结果,该研究结果涉及流经细小多孔介质的流动,其中诱导了高雷诺数。可以提出许多问题:(ⅰ)作者在其摘要中做出了相当明确的断言,即非达西流始于雷诺数4.3,并提出了图7来支持这一主张。实际上,在第12页的“结论”之前的部分中。 524,作者表明,4.3的值来自粘度感应摩擦与总摩擦之比的0.95的任意选择。他们还表明,比率为0.99时,Re = 0.93,而不是Re = 4.3。这与以下事实一致:人们早就认识到,没有Re的单一价值可以说达西定律被打破。在这方面,图7中所示的从线性流到线性后流的过渡的性质与文献中出现的许多其他此类图没有什么不同,并且支持社区认为过渡是渐进的。在以下参考文献中可以找到类似地块的例子:Rose(1945a,b),Ergun(1952),Arbhabhirama和Dinoy(1973)-曲线族,McCorquodale等。 (1978)-大型统一数据集,以及Fand和Thinakaran(1990)-扩展了Reichelt的工作(仅举几例)。尽管这些参考文献的拟合曲线通常比作者的图7散布更多,但无论如何定义摩擦系数和雷诺数项,它们都显示出从线性关系到非线性关系的逐渐过渡。实际上,即使通过管道的流量确实经历了众所周知的突然转变(从层流到部分发展的湍流),也通常认为Re = 2000的数字是一个近似值。因此,抽象论断言非达西流动通过多孔介质是从雷诺数为4.3开始的,这一论点在“结论”部分中再次提出,这是没有道理的。

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