Skip to content
DraconiticResearch
Search Sources API
203,234 studies31 sourcesUpdated 50 min ago
PreprintCC BY-NC-ND 4.0arXiv

The effect of bubble induced turbulent structures on the mass transfer of non-spherical bubbles

Abstract

Although mass transfer from bubbles to liquid is essential for the prediction of the efficiency of reactors, the mass transfer from bubbles is not fully understood. To determine the effect of the local velocity profile on the mass transfer for a wobbling bubble with an Eötvös number of 2 and a Morton number of 10-11, 15 simulations were performed with a Front Tracking method using a sub-grid scale model for the mass transfer in the vicinity of the interface. The vortical structures created by the bubble are influenced by the exact physical properties chosen for the liquid and gas. These changes in the vortical structures also resulted in changes in mass transfer. In addition, the vortical structures created transport barriers between the wake and the bulk of liquid, which were identified by the high-value Finite Time Lyapunov Exponents. These barriers prevent convective mass transfer from the bubble wake to the bulk of the liquid. Therefore, mass transfer from the gas phase to the bulk liquid should take into account both the mass transfer from the gas to the liquid and the transfer from the wake to the bulk of the liquid.

Versions

Related

  1. Turbulent heat transfer and secondary flows in a non-uniformly heated pipe with temperature-dependent fluid properties
    Manuel García-Villalba, A. Antoranz, Oscar Flores
    International Journal of Heat and Fluid FlowPeer-reviewedCC BY3 citedFluid dynamicsHAL
  2. Modelling friction and heat transfer in turbulent forced convection over porous lattices
    Aneek Chakraborty, Stefan Hickel, Davide Modesti
    arXivPreprintCC BY 4.0Full textFluid dynamicsarXiv
  3. Conjugate heat transfer in turbulent pipe flow with azimuthally non-uniform heating
    Jonathan Neuhauser, Davide Gatti, Bettina Frohnapfel
    arXivPreprintCC BY-SA 4.0Full textFluid dynamicsarXiv
  4. Large-Eddy Simulation of the Turbulent Flow and Heat Transfer in a Turbine Vane Model Cooled by Jet Impingement
    Jules Mazaleyrat, Emmanuel Laroche, Remi Manceau +3
    Journal of TurbomachineryPeer-reviewedCC BY-NC-ND 4.0Full textFluid dynamicsHAL
  5. Spectral density of angular momentum transfer from a swift electron to a large spherical nanoparticle
    Jorge Luis Briseño-Gómez, Alejandro Reyes-Coronado
    arXivPreprintarXiv licenceFull textComputational physicsCondensed matterarXiv
BibTeX
@misc{dijke2026effect,
  title = {{The effect of bubble induced turbulent structures on the mass transfer of non-spherical bubbles}},
  author = {Veerle Dijke and Ruben Meijer and Maike Baltussen},
  howpublished = {arXiv},
  year = {2026},
  month = aug,
  doi = {10.48550/arxiv.2605.31285},
  eprint = {2605.31285},
  archivePrefix = {arXiv},
  url = {https://arxiv.org/abs/2605.31285},
  note = {CC BY-NC-ND 4.0},
}
RIS
TY  - UNPB
TI  - The effect of bubble induced turbulent structures on the mass transfer of non-spherical bubbles
AU  - Veerle Dijke
AU  - Ruben Meijer
AU  - Maike Baltussen
PY  - 2026
DA  - 2026/08/21
PB  - arXiv
DO  - 10.48550/arxiv.2605.31285
UR  - https://arxiv.org/abs/2605.31285
AB  - Although mass transfer from bubbles to liquid is essential for the prediction of the efficiency of reactors, the mass transfer from bubbles is not fully understood. To determine the effect of the local velocity profile on the mass transfer for a wobbling bubble with an Eötvös number of 2 and a Morton number of 10-11, 15 simulations were performed with a Front Tracking method using a sub-grid scale model for the mass transfer in the vicinity of the interface. The vortical structures created by the bubble are influenced by the exact physical properties chosen for the liquid and gas. These changes in the vortical structures also resulted in changes in mass transfer. In addition, the vortical structures created transport barriers between the wake and the bulk of liquid, which were identified by the high-value Finite Time Lyapunov Exponents. These barriers prevent convective mass transfer from the bubble wake to the bulk of the liquid. Therefore, mass transfer from the gas phase to the bulk liquid should take into account both the mass transfer from the gas to the liquid and the transfer from the wake to the bulk of the liquid.
ER  -