Contribution of Reynolds stress distribution to the skin friction in wall-bounded flows
By Koji Fukagata, K. Iwamoto, Nobuhide Kasagi. 2002
720 citations recorded by the source corpus.
Subfields: Computational Mechanics, Environmental Engineering, Mechanical Engineering
View Paper: https://www.semanticscholar.org/paper/791351b620f43ccbceb522ef4b25d47cc0cba90e
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In Computational Mechanics
- Sébastien Deck
- Nicolas Renard
- Y. Kametani
- Yuichi Murai
- Koji Fukagata
- Rayhaneh Akhavan
- Bendiks Jan Boersma
- A. Rastegari
In Environmental Engineering
In Mechanical Engineering
Citations in the corpus
- Frictional drag reduction by bubble injection (2014, positive): “Gabillet et al. (2002) found in a horizontal turbulent channel flow with upward bubble injection that the bubbles activated near-wall turbulence that increased linearly with the void fraction.”
- Direct numerical simulation of spatially developing turbulent boundary layers with uniform blowing or suction (2011, methodology): “This somewhat peculiar trend (also found in the blowing/suction slot case by Park & Choi 1999) was explained by an identity equation between the Reynolds stress and the friction drag (Fukagata et al. 2002).”
- The effect of thermal boundary conditions on forced convection heat transfer to fluids at supercritical pressure (2016, background): “The FIK identity was derived by Fukagata et al. (2002) to investigate componential contributions that different dynamical effects have on global integral quantities.”
- On the mechanism of turbulent drag reduction with super-hydrophobic surfaces (2015, background): “Equation (2.3) extends to SH channel flows the analytical formulation originally developed by Fukagata et al. (2002) for the breakdown of skin-friction drag into its constituting elements on smooth no-slip walls, which was later generalized to geometrically complex no-slip surfaces by Peet & Sagaut…”
- A theoretical decomposition of mean skin friction generation into physical phenomena across the boundary layer (2016, methodology): “The weight of the Reynolds shear-stress profile (mean velocity gradient) again significantly differs from the linear weight in the FIK decomposition for a pipe flow (Fukagata et al. 2002).”