Direct numerical simulation of a three-dimensional spatially developing bubble-laden mixing layer with two-way coupling

• Published in: Journal of fluid mechanics Vol. 429; pp. 23 - 61
• Main Authors: DRUZHININ, O. A., ELGHOBASHI, S. E.
• Format: Journal Article
• Language: English
• Published: Cambridge Cambridge University Press 25.02.2001
• Subjects: Bubbles; Entrainment; Exact sciences and technology; Fluctuations; Fluid dynamics; Fluid mechanics; Fundamental areas of phenomenology (including applications); Momentum equation; Multiphase and particle-laden flows; Nonhomogeneous flows; Physics; Upstream; Phase velocity; Three dimensional flow; Two-phase flow; Digital simulation; Vorticity; Hydrodynamic dispersion; Void fraction; Bubble flow; Spherical particle; Vortex pair; Mixing layer
• ISSN: 0022-1120; 1469-7645
• DOI: 10.1017/S0022112000002603

Direct numerical simulations (DNS) of a three-dimensional spatially-developing mixing layer (ML) laden with spherical gaseous bubbles are performed, with both one-way and two-way coupling between the two phases. Forcing is used to initialize the spanwise vortex roll-up and to create a pair of counter-rotating streamwise vortices, rendering the carrier flow three-dimensional. The characteristics of the resulting ML flow field are similar to those reported in numerous experimental and numerical studies. The volume fraction (or concentration) of the bubble phase is considered small enough to neglect bubble–bubble interactions. The no-slip fluid velocity condition is assumed at the bubble surface, and the bubble Reynolds number is less than 1 throughout the simulation time. The two-fluid formulation (TF) is used to compute the bubble-phase velocity and concentration and the two-way coupling source term in the fluid momentum equation. A Lagrangian–Eulerian mapping (LEM) solver is employed to solve the equations for the bubble velocity and concentration. LEM is capable of resolving the gradients of concentration created by the bubble preferential accumulation without numerical instabilities. Two different inflow profiles (Cref(z)) of bubble-phase concentration are considered: a uniform profile and a tanh-profile. In the latter case, the high-speed (upper) stream is devoid of bubbles, and the low-speed (lower) stream is uniformly laden with bubbles at the inflow plane. The DNS results show that in addition to the well-known preferential accumulation of bubbles in the vortex centres, sheets of increased bubble concentration (C-sheets) develop in the rollers created by the vortex pairing in the ML core, with two local maxima of vorticity and an enhanced strain-rate field. The development of C-sheets is governed by the stretching and contraction along the principal axes of the local strain rate. In the case of uniform Cref, the two-way coupling reduces the average ML vorticity thickness and the entrainment of the irrotational fluid into the ML core, as compared to the bubble-free case, upstream of the location of the first vortex pairing. However, both ML vorticity thickness is increased and entrainment is enhanced by the bubbles farther downstream, after the pairing. The fluid velocity fluctuations are reduced by the bubbles throughout the ML, as compared to the one-way coupling case. In the case of the tanh-profile of Cref, the velocity fluctuations and the ML vorticity thickness are increased by the bubbles upstream the location of the first vortex pairing owing to the ‘unstable’ inflow bubble stratification (Druzhinin & Elghobashi 1998). On the other hand, the velocity fluctuations are reduced by the bubbles, and the ML vorticity thickness oscillates with the streamwise distance farther downstream.