Effect of added mass on the interaction of bubbles in a low-Reynolds-number shear flow

被引:3
|
作者
Lavrenteva, Olga [1 ]
Prakash, Jai [1 ]
Nir, Avinoam [1 ]
机构
[1] Technion Israel Inst Technol, Dept Chem Engn, IL-32000 Haifa, Israel
基金
以色列科学基金会;
关键词
COUETTE-POISEUILLE FLOW; TAYLOR VORTEX REACTOR; DRAG REDUCTION; EMULSION POLYMERIZATION; BIOREACTOR; PATTERNS;
D O I
10.1103/PhysRevE.93.023105
中图分类号
O35 [流体力学]; O53 [等离子体物理学];
学科分类号
070204 ; 080103 ; 080704 ;
摘要
Equal size air bubbles that are entrapped by a Taylor vortex of the secondary flow in a Couette device, thereby defying buoyancy, slowly form a stable ordered ring with equal separation distances between all neighbors. We present two models of the process dynamics based on force balance on a bubble in the presence of other bubbles positioned on the same streamline in a simple shear flow. The forces taken into account are the viscous resistance, the added mass force, and the inertia-induced repulsing force between two bubbles in a low-Reynolds-number shear flow obtained in Prakash et al. [J. Prakash et al., Phys. Rev. E 87, 043002 (2013)]. The first model of the process assumes that each bubble interacts solely with its nearest neighbors. The second model takes into account pairwise interactions among all the bubbles in the ring. The performed dynamic simulations were compared to the experimental results reported in Prakash et al. [J. Prakash et al., Phys. Rev. E 87, 043002 (2013)] and to the results of quasistationary models (ignoring the added mass effect) suggested in that paper. It is demonstrated that taking into account the effect of added mass, the models describe the major effect of the bubbles' ordering, provide good estimation of the relaxation time, and also predict nonmonotonic behavior of the separation distance between the bubbles, which exhibit over-and undershooting of equilibrium separations. The latter effects were observed in experiments, but are not predicted by the quasistationary models.
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页数:12
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