Influence of corner geometry on the secondary flow in turbulent square ducts
•The effect of the corner radius on the secondary flow is evaluated.•The cross-flow does not decay in the rounding radius range between r=0 and 0.75.•Cross-flow originates near the curvature change region of the wall.•Inhomogeneous interaction between bursting events leads to cross-flow production....
Gespeichert in:
Veröffentlicht in: | The International journal of heat and fluid flow 2017-10, Vol.67 (PA), p.69-78 |
---|---|
Hauptverfasser: | , , , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
Zusammenfassung: | •The effect of the corner radius on the secondary flow is evaluated.•The cross-flow does not decay in the rounding radius range between r=0 and 0.75.•Cross-flow originates near the curvature change region of the wall.•Inhomogeneous interaction between bursting events leads to cross-flow production.
Direct numerical simulations of fully-developed turbulent flow through a straight square duct with increasing corner rounding radius r were performed to study the influence of corner geometry on the secondary flow. Unexpectedly, the increased rounding of the corners from r=0 to 0.75 does not lead to a monotonic trend towards the pipe case of r=1. Instead, the secondary vortices relocate close to the region of wall-curvature change. This behavior is connected to the inhomogeneous interaction between near-wall bursting events, which are further characterized in this work with the definition of their local preferential direction. We compare our results with those obtained for the flow through a square duct (which corresponds to r=0) and through a round pipe (r=1), focusing on the influence of r on the wall-shear stress distribution and the turbulence statistics along the centerplane and the corner bisector. The former shows that high-speed streaks are preferentially located near the transition between straight and curved surfaces. The Reynolds numbers based on the centerplane friction velocity and duct half-height are Reτ, c ≃ 180 and 350 for the cases under study. |
---|---|
ISSN: | 0142-727X 1879-2278 1879-2278 |
DOI: | 10.1016/j.ijheatfluidflow.2017.07.009 |