Microfluidic step-emulsification in axisymmetric geometry

平面的 旋转对称性 微流控 微通道 机械 无量纲量 毛细管数 毛细管作用 轴对称性 材料科学 分散性 表面张力 管(容器) 相(物质) 几何学 纳米技术 物理 热力学 复合材料 计算机科学 量子力学 计算机图形学(图像) 高分子化学 数学
作者
Indrajit Chakraborty,Joshua Ricouvier,Pavel Yazhgur,Patrick Tabeling,Alexander M. Leshansky
出处
期刊:Lab on a Chip [Royal Society of Chemistry]
卷期号:17 (21): 3609-3620 被引量:37
标识
DOI:10.1039/c7lc00755h
摘要

Biphasic step-emulsification (Z. Li et al., Lab Chip, 2015, 15, 1023) is a promising microfluidic technique for high-throughput production of μm and sub-μm highly monodisperse droplets. The step-emulsifier consists of a shallow (Hele-Shaw) microchannel operating with two co-flowing immiscible liquids and an abrupt expansion (i.e., step) to a deep and wide reservoir. Under certain conditions the confined stream of the disperse phase, engulfed by the co-flowing continuous phase, breaks into small highly monodisperse droplets at the step. Theoretical investigation of the corresponding hydrodynamics is complicated due to the complex geometry of the planar device, calling for numerical approaches. However, direct numerical simulations of the three dimensional surface-tension-dominated biphasic flows in confined geometries are computationally expensive. In the present paper we study a model problem of axisymmetric step-emulsification. This setup consists of a stable core-annular biphasic flow in a cylindrical capillary tube connected co-axially to a reservoir tube of a larger diameter through a sudden expansion mimicking the edge of the planar step-emulsifier. We demonstrate that the axisymmetric setup exhibits similar regimes of droplet generation to the planar device. A detailed parametric study of the underlying hydrodynamics is feasible via inexpensive (two dimensional) simulations owing to the axial symmetry. The phase diagram quantifying the different regimes of droplet generation in terms of governing dimensionless parameters is presented. We show that in qualitative agreement with experiments in planar devices, the size of the droplets generated in the step-emulsification regime is independent of the capillary number and almost insensitive to the viscosity ratio. These findings confirm that the step-emulsification regime is solely controlled by surface tension. The numerical predictions are in excellent agreement with in-house experiments with the axisymmetric step-emulsifier.
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