2022
DOI: 10.1016/j.ces.2022.117543
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Numerical determination of bubble size distribution in Newtonian and non-Newtonian fluid flows based on the complete turbulence spectrum

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Cited by 9 publications
(6 citation statements)
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“…According to previous studies, the breakage mechanism could be classified into four types 4,5 : turbulent eddy impact, viscous shear stress, shearing shedding, and interface instability. Turbulent eddy impact mechanism was widely studied by many researchers 6–21 . Many models of breakage frequency and DSD were proposed by considering different breakage criteria, 6–12 multiple breakage, 13,14 full energy spectrum, 15–18 and internal flow redistribution 19,20 …”
Section: Introductionmentioning
confidence: 99%
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“…According to previous studies, the breakage mechanism could be classified into four types 4,5 : turbulent eddy impact, viscous shear stress, shearing shedding, and interface instability. Turbulent eddy impact mechanism was widely studied by many researchers 6–21 . Many models of breakage frequency and DSD were proposed by considering different breakage criteria, 6–12 multiple breakage, 13,14 full energy spectrum, 15–18 and internal flow redistribution 19,20 …”
Section: Introductionmentioning
confidence: 99%
“…Turbulent eddy impact mechanism was widely studied by many researchers 6–21 . Many models of breakage frequency and DSD were proposed by considering different breakage criteria, 6–12 multiple breakage, 13,14 full energy spectrum, 15–18 and internal flow redistribution 19,20 …”
Section: Introductionmentioning
confidence: 99%
See 1 more Smart Citation
“…Bioprocessing requires gas-liquid mass transfer, particularly with non-Newtonian fluids. Nino et al, [9] recorded bubble diameters in a Rushton turbine-stirred bioreactor to numerically compute and experimentally quantify bubble sizes at different axial locations. In Newtonian (water) and non-Newtonian (0.4% CMC) fluids, viscosity affected bubble dispersion calculations.…”
Section: Introductionmentioning
confidence: 99%
“…Mukhopadhyay et al, [11] used the model of Casson fluid to examine how a non-Newtonian fluid behaved in an unstable twodimensional flow on a stretching surface with a particular surface temperature. The primary objective of Nino et al, [12] was to numerically determine and experimentally compare the diameters of bubbles at various axial positions of a bioreactor being churned by a Rushton turbine. The effects of viscosity on modelling bubble dispersion in a Newtonian fluid (water) and their comparison to a non-Newtonian fluid (0.4% CMC) were particularly highlighted.…”
Section: Introductionmentioning
confidence: 99%