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Generation Mechanisms and Sources of Vorticity Within a Spilling Breaking Wave

机译:溢流爆发波中涡度的产生机理和来源

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Sources of vorticity are examined for a spilling breaking wave. Through the use of a honeycomb/screen section, spilling breaking waves are generated and examined. Two cases were studied. For the first case, based on the breaker height, the Reynolds and Froude numbers were 7370 and 2.04, respectively. The breaker is preceded by 1 mm wavelength capillary waves, with the largest amplitude to wavelength ratio equal to 0.18. For this case, it is found that the dominant source of vorticity flux is a viscous process, and is due to the deceleration of a thin layer of the surface fluid. Furthermore, a thin free surface fluid layer is found to precede wave breaking that moves at a faster speed with respect to the fluid directly beneath it and to the fluid bulk. For the second case, also based on the wave height, the Reynolds and Froude numbers were 1500 and 1.35, respectively. No breaking is observed for this case; rather a capillary-gravity wave is observed with 4 mm wavelength capillaries preceding the gravity wave. The largest amplitude to wavelength ratio of these capillary is 0.28. This case shows that capillary waves do not contribute to the vorticity flux, rather the only dominant source of the vorticity flux into the flow is the free surface fluid deceleration. Lastly, similar to case 1, a thin free-surface fluid layer, which moves faster than the fluid beneath it and to the fluid bulk is found preceding the capillary-gravity wave.
机译:检查涡流的来源是否有溢出的破碎波。通过使用蜂窝/筛网部分,产生并检查溢出的破碎波。研究了两个案例。对于第一种情况,基于断路器高度,雷诺数和弗洛德数分别为7370和2.04。断路器之前是1毫米波长的毛细管波,其最大振幅与波长之比等于0.18。对于这种情况,发现旋涡通量的主要来源是粘性过程,并且归因于表面流体薄层的减速。此外,发现薄薄的自由表面流体层位于波浪破碎之前,该波浪破碎相对于直接在其下方的流体和流体主体以更快的速度运动。对于第二种情况,同样基于波高,雷诺数和弗洛德数分别为1500和1.35。在这种情况下没有观察到破裂。而是在重力波之前观察到毛细管重力波和4 mm波长的毛细管。这些毛细管的最大振幅与波长之比为0.28。这种情况表明,毛细波对旋涡通量没有贡献,而是旋涡通入流中的唯一主要来源是自由表面流体的减速。最后,与情况1相似,在毛细管重力波之前发现了一个薄的自由表面流体层,该流体表面的运动速度快于其下方的流体并到达流体体积。

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