Cavitation in Different Liquids

Cylindrical cavitation between two flat plates is studied for the first time in a shear-thickening particle suspension. Bubble shapes and dynamics are recorded for various volume fractions of the liquid.

Enlarged view: Cylindrical bubbles in water and cornstarch suspensions with different concentrations.
Selected frames from 125 kFPS visualizations of nominally cylindrical spark-induced bubbles in (a) water, and in cornstarch suspensions of volume fractions (b) φ = 0.37, (c) φ = 0.44, (d) φ = 0.46, and (e) φ = 0.52. Every sequence shows instants t = 0.32, 0.80, 1.28, 1.60, 1.92, 2.24, and 2.32 ms, with t = 0 ms defined as spark ignition. The brightness of all frames has been increased.

Cavitation has been extensively studied in Newtonian fluids and to a lesser yet significant degree in shear-thinning fluids. However, cavitation has not been previously investigated in shear-thickening fluids, of which a water-cornstarch suspension is perhaps the best-known example. An interesting property of such fluids is that, when subjected to an increase in strain rate, their viscosity increases until they exhibit solidlike behavior and can even fracture. As cavitation bubbles are capable of generating extreme strain rates, they could be affected by shear-thickening fluid behavior. As visual access is limited by opaque or non-index-matched particles present in such fluids, an experimental study of nominally cylindrical spark-induced cavitation bubbles is conducted in a 2 mm gap between two parallel flat and transparent plates, which allows visualization of the bubbles as they contact the boundary. They are theoretically studied through the cylindrical Keller-Miksis equation adapted to a shear-thickening fluid using a Cross model. For volume fractions starting from φ = 0.44, the limit between continuous and discontinuous shear-thickening regime, cavitation bubbles deform increasingly until they are replaced by cavitation-induced fracture between φ = 0.46 and φ = 0.52. Fracture propagation speeds were found to be in the same range as fracture speeds previously reported for pressure-driven cavity expansion, albeit for estimated initial pressures that are now orders of magnitude higher. More details can be found in our external page study.

Enlarged view: Mean fracture speed and aspect ratio of cavitation-induced fracture in shear-thickening fluid.
Mean fracture speed (top) and aspect ratio (bottom) of cavitation-induced fracture in a shear-thickening fluid (cornstarch suspension of φ = 0.52) for different maximum radii Rmax. The color of the symbols indicates the estimated initial gas pressure generated by the spark, and the dash-dotted line shows the mean value for the aspect ratio. Images of different fracture patterns for a capacitor charged at (a) 60 V and showing the wire electrodes, (b) 70 V, and (c) 90 V, are visible, as well as (d) image showing the equivalent circular area computed from the dark pixels of the fracture shape in image (b). The circle shows the maximum radius, Rmax. The uncertainty on v and A are indicated by error bars sometimes hidden by their marker.
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