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According to Nakahara (private communication), a typical value of the Reynolds number in such cases is RH =100 on the basis of the layer thickness H, or RL =2000 on the basis of the horizontal length scale L of the container. While RH =100 is typically not large enough to cause a transition to turbulence (in the usual sense of the word), we may expect a different kind of "turbulence" such as a two-dimensional chaotic flow maintained by horizontal forcing.
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According to Nakahara (private communication), a typical value of the Reynolds number in such cases is RH =100 on the basis of the layer thickness H, or RL =2000 on the basis of the horizontal length scale L of the container. While RH =100 is typically not large enough to cause a transition to turbulence (in the usual sense of the word), we may expect a different kind of "turbulence" such as a two-dimensional chaotic flow maintained by horizontal forcing.
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The presence of the viscous drag is not explicitly stated in Duran's book, but it seems to be implicitly assumed by stating that x stops at the position satisfying kx=mGsinθ.
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The presence of the viscous drag is not explicitly stated in Duran's book, but it seems to be implicitly assumed by stating that x stops at the position satisfying kx=mGsinθ.
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