Experimental validation of RANS and DES modelling of pipe flow mixing
Velocity and concentration profiles in a pipe flow was measured downstream of injection of a tracer gas at the pipe centerline. The pipe had diameter D = 0.2 m and two Reynolds numbers, Re = 50000 and Re = 100000, were used. The profiles were measured at positions 5 D and 10 D downstream of the inje...
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Veröffentlicht in: | Heat and mass transfer 2020-07, Vol.56 (7), p.2211-2224 |
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Format: | Artikel |
Sprache: | eng |
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Zusammenfassung: | Velocity and concentration profiles in a pipe flow was measured downstream of injection of a tracer gas at the pipe centerline. The pipe had diameter
D
= 0.2 m and two Reynolds numbers, Re = 50000 and Re = 100000, were used. The profiles were measured at positions 5
D
and 10
D
downstream of the injection point. Three different industrial relevant geometrical configurations were used upstream of the injection point: a 10
D
straight pipe, two 10
D
pipes connected with a 90° bend or a straight 10
D
pipe with a mixer plate mounted 2
D
upstream the injection point. In all cases, air entered the pipe from the surroundings through a sharp-edged inlet. This represents many practical flow applications and is also a well-defined inlet condition that generates turbulence in the
vena contracta
in the inlet. The measurements were compared to predictions from three different computational models: two with Reynolds Averaged Navier-Stokes (RANS) and one with high-resolution Detached Eddy Simulation (DES). For RANS, the k-
ω
SST model had difficulty in predicting the turbulence created by the
vena contracta
. The k-
ε
model performed better, but gave completely wrong results for the inlet with a pipe bend. The DES was successful for all cases with only minor deviations from measurements. |
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ISSN: | 0947-7411 1432-1181 |
DOI: | 10.1007/s00231-020-02835-8 |