Channel flow benchmarks
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Transcript Channel flow benchmarks
Channel flow benchmarks
•
DNS datasets to validate Code_Saturne
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Effect of complex grids
hexa, non-conform, tetra
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Low Reynolds number tests Ret = 100
no turbulence model
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Ret = 395 tests
subgrid scale model tests
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Towards high Reynolds numbers
subgrid scale models at high Reynolds
numbers
Channel flow benchmarks: « classic » DNS
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DNS Ret = 180
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Box 4 x 2 x 2, Grid 192 x 128 x 160 (4M cells)
Same grid as Mansour, Kim & Moin
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Results include
velocity, shear and normal stresses (<u>, <u’v’> etc… )
Triple correlations (<v’u’u’> etc…)
Terms in turbulent kinetic energy budget
Terms in the components of each budget
Channel flow benchmarks: DNS Ret =180
• Grid adapted for a
spectral code
• but applied to a non
spectral code
Channel flow benchmarks: DNS Ret =180
• Grid adapted for a spectral code
• but applied to a non spectral code
Channel flow benchmarks: DNS Ret =180
• Grid adapted for a spectral code
• but applied to a non spectral code
Channel flow benchmarks: DNS Ret =180
Channel flow benchmarks: DNS Ret =180
Channel flow benchmarks: DNS Ret =180
Channel flow benchmarks: Code_Saturne test grids
Hexahedral
Non-conform (hexa)
Box 2 x 2 x
440,000 elements
Tetrahedral
Channel flow benchmarks: Ret = 100
• DNS 880k cells
for same box size
• tests 440k cells
• Tetra
poorly resolved
difference in grid on
each wall
• Hexa
too coarse at wall
Channel flow benchmarks: Ret = 100
• turbulence kinetic energy
• weaknesses of each case become more clear
Channel flow benchmarks: Ret = 395
• velocity
Channel flow benchmarks: Ret = 395
• shear stress
Channel flow benchmarks: Ret = 395
• normal stresses
Channel flow benchmarks: Ret = 395
• tke
Channel flow benchmarks: high Reynolds numbers
• Box 6 x 2 x2, Grid 11 x 11 x 11 (1.3k cells)
Detail of the tubes that make up a bundle inside a SFR reactor
Thermal
radiation
Ensure the tubes don’t touch,
Ensure that sodium cannot get trapped (particularly
important with respect to the neutronic reactions),
Reduce vibrations within the tube bundle,
Improve the mixing near the heater and increase the rate
of heat exchange.
First attempts to simulate the fluid
A z=100mm
A z=140mm