4.7 Article

A deformable liquid drop falling through a quiescent gas at terminal velocity

Journal

JOURNAL OF FLUID MECHANICS
Volume 658, Issue -, Pages 438-462

Publisher

CAMBRIDGE UNIV PRESS
DOI: 10.1017/S0022112010001825

Keywords

aerosols/atomization; drops and bubbles; interfacial flows (free surface)

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The steady axisymmetric flow internal and external to a deformable viscous liquid drop falling through a quiescent gas under the action of gravity is computed by solving the nonlinear Navier-Stokes equations using a Galerkin finite-element method with a boundary-fitted quadrilateral mesh. Considering typical values of the density and viscosity for common liquids and gases, numerical solutions are first computed for the liquid-to-gas density ratio rho = 1000 and viscosity ratio mu from 50 to 1000. Visually noticeable drop deformation is shown to occur when the Weber number We similar to 5. For mu >= 100, drops of Reynolds number Re < 200 tend to have a rounded front and flattened or even dimpled rear, whereas those at Re > 200 a flattened front and somewhat rounded rear, with that at Re = 200 exhibiting an almost fore-aft symmetric shape. As an indicator of drop deformation, the axis ratio (defined as drop width versus height) increases with increasing We and mu, but decreases with increasing Re. By tracking the solution branches around turning points using an arclength continuation algorithm, critical values of We for the 'shape instability' are determined typically within the range of 10 to 20, depending on the value of Re (for Re >= 100). The drop shape can change drastically from prolate-to oblate-like when mu < 80 (for 100 <= Re <= 500). For example, for mu = 50 a drop at Re >= 200 exhibits a prolate shape when We < 10 and an upside-down button mushroom shape when We > 10. The various solutions computed at rho = 1000 with the associated values of drag coefficient and drop shapes are found to be almost invariant at other values of rho (e. g. from 500 to 1500) as long as the value of rho/mu(2) is fixed, despite the fact that the internal circulation intensity changes according to the value of mu. The computed values of drag coefficient are shown to agree quite well with an empirical formula for rigid spheres with the radius of the sphere replaced by the radius of the cross-sectional area.

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