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Research Article | Open Access

Experimental and numerical study on the transport of dilute bubbles in a T-junction channel flow

Erik Frense1( )Xinghao Yang1,2Frank Rüdiger1Mark-Patrick Mühlhausen2Jochen Fröhlich1
Institute of Fluid Mechanics, Technische Universität Dresden, George-Bähr-Strasse 3c, 01069 Dresden, Germany
CoC Fluid Dynamics, Bosch Rexroth, Partensteiner Str. 23, 97816 Lohr am Main, Germany
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Abstract

The present study investigates the transport of dilute bubbles by transitional flow in a joining, cross-flow-type T-junction channel geometry with Reynolds numbers at the outlet branch from Re3 = 600 to 1800 and an inlet volume flow rate ratio of 1. Bubbles with diameters between db = 400 and 600 μm are considered. The schematic pattern of the single-phase flow is introduced based on streakline dye visualizations. Complex 3D flow due to the narrow channel design dominates the recirculation area and flow instabilities become important with increasing Reynolds number, which can be observed by the fading of dye intensity. A numerical method is presented with unsteady boundary conditions based on laser Doppler velocimetry measurements. Bubble trajectories are obtained by an Euler–Lagrange approach. Using high-speed shadowgraphy method combined with image processing, bubble sizes were measured, and bubble trajectories were evaluated. Experimental bubble trajectories and numerically predicted bubble positions show good agreement for Re3 = 600, which is also the case with the dye visualization image. For higher Reynolds numbers, measurements of the bubble trajectories are reported and compared to dye visualization images. The increasing flow instabilities influence the bubble transport, resulting in large variations of bubble locations.

References

 
Brennen, C. E. 2005. Fundamentals of Multiphase Flow. Cambridge: Cambridge University Press.
 
Chesters, A. 1991. The modelling of coalescence processes in fluid–liquid dispersions: A review of current understanding. Chemical Engineering Research & Design, 69: 259270.
 
Christopher, G. F., Anna, S. L. 2007. Microfluidic methods for generating continuous droplet streams. Journal of Physics D: Applied Physics, 40: R319R336.
 
Costa, N. P., Maia, R., Proença, M. F., Pinho, F. T. 2006. Edge effects on the flow characteristics in a 90 deg tee junction. Journal of Fluids Engineering, 128: 12041217.
 
Crocker, J. C., Grier, D. G. 1996. Methods of digital video microscopy for colloidal studies. Journal of Colloid and Interface Science, 179: 298310.
 
Czarske, J. R., Büttner, L., Razik, T., Müller, H. 2002. Boundary layer velocity measurements by a laser Doppler profile sensor with micrometre spatial resolution. Measurement Science and Technology, 13: 19791989.
 
Drenckhan, W., Langevin, D. 2010. Monodisperse foams in one to three dimensions. Current Opinion in Colloid & Interface Science, 15: 341358.
 
Frense, E., Werner, T., Nöpel, J.-A., Rüdiger, F. 2022. Detection and evaluation of single bubble collisions using focused shadowgraphy. In: Proceedings of the 29th Symposium of Experimental Fluid Mechanics of GALA e.V., 17.417.8. Available at https://www.gala-ev.org/images/Beitraege/Beitraege2022/pdf/17.pdf.
 
Garstecki, P., Fuerstman, M. J., Stone, H. A., Whitesides, G. M. 2006. Formation of droplets and bubbles in a microfluidic T-junction-scaling and mechanism of break-up. Lab Chip, 6: 437446.
 
Gholizadeh, H., Burton, R., Schoenau, G. 2012. Fluid bulk modulus: Comparison of low pressure models. International Journal of Fluid Power, 13: 716.
 
Heitkam, S., Sommer, A. E., Drenckhan, W., Fröhlich, J. 2017. A simple collision model for small bubbles. Journal of Physics: Condensed Matter, 29: 124005.
 
Hoppe, F., Breuer, M. 2018. A deterministic and viable coalescence model for Euler–Lagrange simulations of turbulent microbubble-laden flows. International Journal of Multiphase Flow, 99: 213230.
 
Hoppe, F., Breuer, M. 2020. A deterministic breakup model for Euler–Lagrange simulations of turbulent microbubble-laden flows. International Journal of Multiphase Flow, 123: 103119.
 
Kamp, A. M., Chesters, A. K., Colin, C., Fabre, J. 2001. Bubble coalescence in turbulent flows: A mechanistic model for turbulence-induced coalescence applied to microgravity bubbly pipe flow. International Journal of Multiphase Flow, 27: 13631396.
 
Legendre, D., Magnaudet, J. 1998. The lift force on a spherical bubble in a viscous linear shear flow. Journal of Fluid Mechanics, 368: 81126.
 
Liao, Y., Lucas, D. 2009. A literature review of theoretical models for drop and bubble breakup in turbulent dispersions. Chemical Engineering Science, 64: 33893406.
 
Liao, Y., Lucas, D. 2010. A literature review on mechanisms and models for the coalescence process of fluid particles. Chemical Engineering Science, 65: 28512864.
 
Müller-Fischer, N., Tobler, P., Dressler, M., Fischer, P., Windhab, E. J. 2008. Single bubble deformation and breakup in simple shear flow. Experiments in Fluids, 45: 917926.
 
Nöpel, J. A., Frense, E., Korb, S., Dues, M., Rüdiger, F. 2019. Velocity measurement of a free jet in water with shear layer cavitation. In: Proceedings of the 27th Symposium of Experimental Fluid Mechanics of GALA e.V., 38.138.8. Available at https://www.gala-ev.org/images/Beitraege/Beitraege2019/pdf/38.pdf.
 
Patiño-Jaramillo, G. A., Iglesias, I., Vera, M. 2022. Laminar flow and pressure loss in planar Tee joints: Numerical simulations and flow analysis. European Journal of Mechanics - B/Fluids, 92: 7589.
 
Pollack, G. L. 1991. Why gases dissolve in liquids. Science, 251: 13231330.
 
Ramamurthy, A. S., Zhu, W. 1997. Combining flows in 90° junctions of rectangular closed conduits. Journal of Hydraulic Engineering, 123: 10121019.
 
Ruan, J., Burton, R. 2007. Bulk modulus of air content oil in a hydraulic cylinder. In: Proceedings of the ASME 2006 International Mechanical Engineering Congress and Exposition, 259269.
 
Takagi, S., Matsumoto, Y. 2010. Surfactant effects on bubble motion and bubbly flows. Annual Review of Fluid Mechanics, 43: 615636.
 
Takemura, F., Magnaudet, J. 2003. The transverse force on clean and contaminated bubbles rising near a vertical wall at moderate Reynolds number. Journal of Fluid Mechanics, 495: 235253.
 
Tomiyama, A., Kataoka, I., Zun, I., Sakaguchi, T. 1998. Drag coefficients of single bubbles under normal and micro gravity conditions. JSME International Journal Series B, Fluids and Thermal Engineering, 41: 472479.
 
Van der Walt, S., Schönberger, J. L., Nunez-Iglesias, J., Boulogne, F., Warner, J. D., Yager, N., Gouillart, E., Yu, T. 2014. Scikit-image: Image processing in Python. PeerJ, 2: e453.
 
Yang, X., Mühlhausen, M. P., Fröhlich, J. 2021a. Interpolation methods for two-way coupled Euler–Lagrange simulation of finite-size bubbles. Chemical Engineering Science, 238: 116566.
 
Yang, X., Mühlhausen, M. P., Fröhlich, J. 2021b. Efficient simulation of bubble dispersion and resulting interaction. Experimental and Computational Multiphase Flow, 3: 152170.
Experimental and Computational Multiphase Flow
Pages 396-410
Cite this article:
Frense E, Yang X, Rüdiger F, et al. Experimental and numerical study on the transport of dilute bubbles in a T-junction channel flow. Experimental and Computational Multiphase Flow, 2023, 5(4): 396-410. https://doi.org/10.1007/s42757-022-0156-4

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Received: 05 August 2022
Revised: 03 December 2022
Accepted: 25 December 2022
Published: 19 April 2023
© The Author(s) 2023

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