Abstract

Temporal instabilities of a planar liquid jet are studied using direct numerical simulation (DNS) of the incompressible Navier–Stokes equations with level-set (LS) and volume-of-fluid (VoF) surface tracking methods. $\unicode[STIX]{x1D706}_{2}$ contours are used to relate the vortex dynamics to the surface dynamics at different stages of the jet breakup – namely, lobe formation, lobe perforation, ligament formation, stretching and tearing. Three distinct breakup mechanisms are identified in the primary breakup, which are well categorized on the parameter space of gas Weber number ($We_{g}$) versus liquid Reynolds number ($Re_{l}$). These mechanisms are analysed here from a vortex dynamics perspective. Vortex dynamics explains the hairpin formation, and the interaction between the hairpins and the Kelvin–Helmholtz (KH) roller explains the perforation of the lobes, which is attributed to the streamwise overlapping of two oppositely oriented hairpin vortices on top and bottom of the lobe. The formation of corrugations on the lobe front edge at high $Re_{l}$ is also related to the location and structure of the hairpins with respect to the KH vortex. The lobe perforation and corrugation formation are inhibited at low $Re_{l}$ and low $We_{g}$ due to the high surface tension and viscous forces, which damp the small-scale corrugations and resist hole formation. Streamwise vorticity generation – resulting in three-dimensional instabilities – is mainly caused by vortex stretching and baroclinic torque at high and low density ratios, respectively. Generation of streamwise vortices and their interaction with spanwise vortices produce the liquid structures seen at various flow conditions. Understanding the liquid sheet breakup and the related vortex dynamics are crucial for controlling the droplet-size distribution in primary atomization.

Highlights

  • Earlier computational works on the breakup of liquid streams at higher Weber number (W e) and Reynolds number (Re) focused on the surface dynamics using either volume-of-fluid or level-set methods (Shinjo & Umemura 2010; Desjardins & Pitsch 2010; Herrmann 2011)

  • Hussain mechanisms were identified and their zones of occurrence were specified on the gasphase Weber number (W eg) versus liquid-phase Reynolds number (Rel) map; (ii) the most important actions in each of the three breakup domains were explained; (iii) the effects of density ratio, viscosity ratio, and sheet thickness on the breakup domains were described; (iv) characteristic times for each of these breakup domains were correlated with key parameters; and (v) the same breakup domains were shown to apply for round jets and planar jets with a very similar W eg versus Rel map

  • The present study has focused mainly on the vortex dynamics of planar liquid jets

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Summary

Introduction

Earlier computational works on the breakup of liquid streams at higher Weber number (W e) and Reynolds number (Re) (i.e. in the atomization range) focused on the surface dynamics using either volume-of-fluid or level-set methods (Shinjo & Umemura 2010; Desjardins & Pitsch 2010; Herrmann 2011). Hussain mechanisms were identified and their zones of occurrence were specified on the gasphase Weber number (W eg) versus liquid-phase Reynolds number (Rel) map; (ii) the most important actions in each of the three breakup domains were explained; (iii) the effects of density ratio, viscosity ratio, and sheet thickness on the breakup domains were described; (iv) characteristic times for each of these breakup domains were correlated with key parameters; and (v) the same breakup domains were shown to apply for round jets and planar jets with a very similar W eg versus Rel map

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