Scaling of Convective Heat Transfer in Laminar and Turbulent Wall Jets With Effects of Freestream Flow and Forcing
Abstract (Summary)
Despite its importance as a canonical two-dimensional flow, the laminar wall jet
has not been extensively studied using modern computational fluid dynamic methods.
The plane laminar wall jet with a specified velocity profile at the jet exit is numerically
investigated. In these types of flows in which the flow field evolves to its self-similar
behavior, the location of the dimensionless hydrodynamic virtual origin is carefully
investigated and expressed as a function of Reynolds number for uniform and parabolic
jet profiles. The local skin friction coefficient is observed to converge to the analytical
self-similar solution at downstream locations. Since no analytical solution exists for the
temperature field in either the developing or self-similar regions of this problem, the
thermal solution is investigated for both isothermal and isoflux boundary conditions at
the wall. The dimensionless thermal virtual origin is correlated as a function of Reynolds
number. The Nusselt number dependence on Prandtl number, Reynolds number and the
downstream location are obtained for both jet profiles and wall boundary conditions.
The turbulent wall jet is experimentally investigated for jet Reynolds number
varying between 6000 and 10000. The effect of the free stream on the wall jet film
cooling effectiveness and on the local heat transfer are investigated for blowing ratio
varying between 2.4 to infinity. The local Nusselt number dependence on Reynolds
number and on the downstream location is identified and the obtained results are
correlated for the various considered blowing ratios. The forcing effect reveals a dramatic
reduction in the film cooling effectiveness which is more pronounced in the absence of a
free stream flow. The Nusselt number decreases with increasing forcing amplitude and
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frequency in the vicinity of the jet exit, however, at further downstream locations an
inflection point is observed in the Nusselt number decay with the streamwise direction
which results in a larger Nusselt number value than the one observed in the unforced
case. The inflection point is not seen in the presence of a free stream flow.
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Bibliographical Information:
Advisor:
School:The University of Arizona
School Location:USA - Arizona
Source Type:Master's Thesis
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