Literature DB >> 28944810

Microfluidic step-emulsification in axisymmetric geometry.

I Chakraborty1, J Ricouvier, P Yazhgur, P Tabeling, A M Leshansky.   

Abstract

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.

Entities:  

Year:  2017        PMID: 28944810     DOI: 10.1039/c7lc00755h

Source DB:  PubMed          Journal:  Lab Chip        ISSN: 1473-0189            Impact factor:   6.799


  2 in total

1.  Numerical simulations of wall contact angle effects on droplet size during step emulsification.

Authors:  Meng Wang; Chuang Kong; Qisen Liang; Jianxiang Zhao; Maolin Wen; Zhongbin Xu; Xiaodong Ruan
Journal:  RSC Adv       Date:  2018-09-25       Impact factor: 4.036

2.  Split or slip - passive generation of monodisperse double emulsions with cores of varying viscosity in microfluidic tandem step emulsification system.

Authors:  Adam S Opalski; Karol Makuch; Ladislav Derzsi; Piotr Garstecki
Journal:  RSC Adv       Date:  2020-06-16       Impact factor: 3.361

  2 in total

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