Heat transfer in turbulent flows with Lagrangian methods: scales of turbulent tranport in wall turbulence

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dc.contributor.author Papavassiliou, D.V.
dc.contributor.author Srinivasan, C.
dc.date.accessioned 2014-12-09T11:39:45Z
dc.date.available 2014-12-09T11:39:45Z
dc.date.issued 2012
dc.description.abstract Paper presented at the 9th International Conference on Heat Transfer, Fluid Mechanics and Thermodynamics, Malta, 16-18 July, 2012. en_US
dc.description.abstract We use a Lagrangian computational methodology that allows the calculation of statistical quantities in turbulent heat transfer. The study utilizes a direct numerical simulation (DNS) of turbulent flow in an infinite channel and in plane Couette flow, in conjunction with the Lagrangian scalar tracking method (LST). The computational box dimensions are 4πh × 2h × 2πh in x, y, z for Poiseuille flow and 8πh × 2h × 2πh for Couette flow (where h is the half channel height). The transport of heat is simulated with LST, which involves the tracking of the trajectories of heat markers in the flow generated by the DNS. The effects of convection are simulated by moving the markers under the assumption that they follow the velocity field. The diffusion effect is simulated by adding a 3D random walk on the particle motion that follows a normal distribution with a standard deviation that depends on the Prandtl number, Pr, of the fluid [1]. The range of Pr covers a wide range (between 0.1 and 6). The trajectories of about 150,000 heat markers are calculated for each case. These trajectories are then used to obtain turbulent dispersion data and to obtain the correlation coefficients for single particle and for relative particle pair dispersion. In addition, the dispersion backwards in time was considered. This was motivated by recent studies about backwards dispersion that have shown differences with forwards turbulent dispersion. The results show differences in the rates of forwards and backwards dispersion [2]. The time scales that are important to turbulent transport and for mixing are thus revealed. Differences between Couette flow and Poiseuille flow highlight the effects of the velocity structure of the turbulence next to the wall on the transport of heat. The presentation will present the numerical methodology and results will be compared with available data from earlier DNS works [3,4]. en_US
dc.description.librarian dc2014 en_US
dc.format.extent 5 pages en_US
dc.format.medium PDF en_US
dc.identifier.citation Papavassiliou, DV & Srinivasan, C 2012, Heat transfer in turbulent flows with Lagrangian methods: scales of turbulent tranport in wall turbulence, Paper presented to the 9th International Conference on Heat Transfer, Fluid Mechanics and Thermodynamics, Malta, 16-18 July, 2012. en_US
dc.identifier.isbn 9781868549863
dc.identifier.uri http://hdl.handle.net/2263/42875
dc.language.iso en en_US
dc.publisher International Conference on Heat Transfer, Fluid Mechanics and Thermodynamics en_US
dc.relation.ispartof HEFAT 2012 en_US
dc.rights University of Pretoria en_US
dc.subject Lagrangian computational methodology en_US
dc.subject Turbulent heat transfer en_US
dc.subject Direct numerical simulation en_US
dc.subject DNS en_US
dc.subject Turbulent flow en_US
dc.subject Couette flow en_US
dc.subject Lagrangian scalar tracking en_US
dc.subject LST en_US
dc.subject Diffusion effect en_US
dc.subject Backwards dispersion en_US
dc.subject Forwards turbulent dispersion en_US
dc.subject Poiseuille flow en_US
dc.title Heat transfer in turbulent flows with Lagrangian methods: scales of turbulent tranport in wall turbulence en_US
dc.type Presentation en_US


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