Direct numerical simulation of turbulent pipe flow up to Re<sub>τ</sub>=5200
ORAL
Abstract
Well-resolved direct numerical simulations (DNSs) of a turbulent pipe flow were conducted at several friction Reynold numbers up to Reτ=5200. The axial domain has a length of 10πR, with 12288×1024×5120 grid points in axial, radial, and azimuthal directions, respectively, following standard DNS resolution. We employ the open-source code “OPENPIPE”, using a Fourier-Galerkin method in the axial and azimuthal directions, and a central finite difference scheme with a 9-point stencil in the wall-normal direction. Turbulence statistics have been obtained, and a clear Reynolds number dependency is documented and compared with other DNS data in pipes as well as channels. In particular, the mean pressure is the quantity that found to differ notably between pipes and channels – linked to the different geometry in the outer wake region. In addition, the pressure fluctuations in the pipe are higher than that in the channel, but the difference progressively decreases as Re increases. The inner peak of the axial velocity fluctuation and the wall-shear stress rms for the pipe, which is slightly lower than for the channel, continuously increase with Reτ as in all other wall flows. Confidence intervals for the the various statistical quantities are also provided to assess the fidelity of the current data.
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Presenters
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Jie Yao
Texas Tech University
Authors
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Jie Yao
Texas Tech University
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Philipp Schlatter
SimEx/FLOW, KTH Engineering Mechanics, Royal Institute of Technology, Stockholm, Sweden, KTH Royal Institute of Technology, SimEx/FLOW, KTH Engineering Mechanics
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Saleh Rezaeiravesh
SimEx/FLOW, KTH Engineering Mechanics, Royal Institute of Technology, Stockholm, Sweden, KTH Royal Institute of Technology
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Fazle Hussain
Texas Tech Univ