EventsMicromachines 2021 — 1st International Conference on Micromachines and Applications (ICMA2021)
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This submission belongs to the session S2. Microfluidic micromachines of the event Micromachines 2021 — 1st International Conference on Micromachines and Applications (ICMA2021)
Published date
16 Apr, 2021
Citation
Maryam Fatehifar, Masoud Jabbari, Alistair Revell, Droplet formation in a cross-junction microfluidic channel with non-Newtonian dispersed phase, in Proceedings of Micromachines 2021 — 1st International Conference on Micromachines and Applications (ICMA2021), 15 April–30 April 2021, MDPI: Basel, Switzerland, doi: 10.3390/Micromachines2021-09588
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Droplet formation in a cross-junction microfluidic channel with non-Newtonian dispersed phase

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Masoud Jabbari 2
1. Department of Mechanical, Aerospace and Civil Engineering, The University of Manchester, Manchester M13 9PL, UK, UK
2. Department of Mechanical, Aerospace and Civil Engineering, The University of Manchester, Manchester M13 9PL, UK
Abstract

Microfluidics enables generating series of isolated droplets for high-throughput screening. As many biological/chemical solutions are of shear thinning non-Newtonian nature [1,2], we studied non-Newtonian droplet generation to improve the reliability of simulation results in real-life assays. We considered non-Newtonian power-law behaviour for Xanthan gum aqueous solution as the dispersed phase, and Newtonian canola oil as the continuous phase. Simulations were performed in OpenFOAM, using the interFoam solver and volume of fluid (VOF) method [3].

A cross-junction geometry with each inlet and outlet channel height (H) and width (W) equal to 50 micrometers with slight contractions in the conjunctions was used to gain a better monodispersity. Following validation of the numerical setup, we conducted a series of tests to provide novel insight into this configuration.

With Capillary number, of 0.01, dispersed phase to continuous phase flow-rate ratio of 0.05, and contact angle of 160˚, simulations revealed that by increasing the Xanthan gum concentration (0, 800, 1500, 2500 ppm) or in other words, decreasing the n -flow behaviour index- from 1 to 0.491, 0.389, and 0.302 in power-law model [4] : (a) breakup of the dispersed phase thread occurred at 0.0365, 0.0430, 0.0440, 0.0450 s; (b) the dimensionless width of the thread at the main channel entrance increased from 0 to 0.066, 0.096, 0.16; and (c) the dimensionless droplet diameter decreased from 0.76 to 0.72, 0.68, 0.67, respectively. Our next plan is to study effect of shear-thinning behaviour on droplet generation in different Ca and flow-rate ratios.

References

  1. Eun, Y.; Utada, A.S.; Copeland, M.F.; Takeuchi, S.; Weibel, D.B. Encapsulating Bacteria in Agarose Microparticles Using Microfluidics for High-Throughput Cell Analysis and Isolation. ACS Chem. Biol. 2011, 6, 260–266, doi:10.1021/cb100336p.
  2. Khater, A.; Khater, A.; Abdelrehim, O.; Mohammadi, M.; Mohammadi, M.; Mohammadi, M.; Azarmanesh, M.; Azarmanesh, M.; Janmaleki, M.; Salahandish, R.; et al. Picoliter agar droplet breakup in microfluidics meets microbiology application: Numerical and experimental approaches. Lab Chip 2020, 20, 2175–2187, doi:10.1039/d0lc00300j.
  3. Chen, Q.; Li, J.; Song, Y.; Christopher, D.M.; Li, X. Modeling of Newtonian droplet formation in power-law non-Newtonian fluids in a flow-focusing device. Heat Mass Transf. 2020, 56, 2711–2723, doi:10.1007/s00231-020-02899-6.
  4. Taassob, A.; Manshadi, M.K.D.; Bordbar, A.; Kamali, R. Monodisperse non-Newtonian micro-droplet generation in a co-flow device. J. Brazilian Soc. Mech. Sci. Eng. 2017, 39, 2013–2021, doi:10.1007/s40430-016-0699-z.
Keywords
simulation
droplet microfluidics
non-Newtonian fluid
volume of fluid
Oral Presentation
Poster
Fatehifar et al..pdf
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