cyclonWizard,
I agree that the Nusselt number will increase as the flow velocity increases in normal flows... which will effect the heat transfer coefficent. My point is that in the reynold calculation that you have shown is overly simplified and does not simulate the actual effects of the jet turbulence.
The flow is laminar exiting the nipple of the waterblock... I think we can both agree with. However, the nipple acts as a trip, increasing the turbulence of the water flow. The boundary layer seperates and the jet of water impacts directly upon the waterblock.
In an impinging jet flow, most turbulation models do not accuratly predict the mean velocity and reynold stress preditions in the near-wall region of the flow. At distances well removed from the point of impingement the Nusselt number predictions are accurate... however due to failure to show acceleration of the flow along the impingement plate, the heat transfer predictions are poor. This is due to the assumptions in 2 equation turbulence models. The jet flow, after exiting the nipple, undergoes streamline curvature and is subjected to strong deceleration as the fluid nears the impingment plate. After the jet impinges on the plate, the fluid accelerates radially, forming a 3 dimensional flow field. Turbulent vortices generated in the jet shear layer will be streatched parallel to the plate after impingement, altering the turbulent length scale of the flow. 2 equation turbulence models assume a linear stress-strain relation and a length scale based on thin shear layer approximations. Therefore, these equations can be expected to perform poorly near the point of impingment where these assumptions are not valid. At locations well removed from the point of impingement, the flow approximates that of a 2D boundary layer and the 2 equation models of turbulence perform reasonable well. [copied without permission from the CFD society of Canada] http://www.cfdsc.ca/english/benchmarks/cfd95/node1.html
I believe, based on the above the although velocity will or can have some effect on the turbulation of the flow and thus the heat transfer... the equations that you are showing are incorrect... and in fact that the effects of a velocity increase are negligible when compared to the rapid decelleration and turbulation caused by the jet hitting the waterblock.
And yes... I am an engineer... even if my spelling sucks... they need a spell checker in this thing!!
I agree that the Nusselt number will increase as the flow velocity increases in normal flows... which will effect the heat transfer coefficent. My point is that in the reynold calculation that you have shown is overly simplified and does not simulate the actual effects of the jet turbulence.
The flow is laminar exiting the nipple of the waterblock... I think we can both agree with. However, the nipple acts as a trip, increasing the turbulence of the water flow. The boundary layer seperates and the jet of water impacts directly upon the waterblock.
In an impinging jet flow, most turbulation models do not accuratly predict the mean velocity and reynold stress preditions in the near-wall region of the flow. At distances well removed from the point of impingement the Nusselt number predictions are accurate... however due to failure to show acceleration of the flow along the impingement plate, the heat transfer predictions are poor. This is due to the assumptions in 2 equation turbulence models. The jet flow, after exiting the nipple, undergoes streamline curvature and is subjected to strong deceleration as the fluid nears the impingment plate. After the jet impinges on the plate, the fluid accelerates radially, forming a 3 dimensional flow field. Turbulent vortices generated in the jet shear layer will be streatched parallel to the plate after impingement, altering the turbulent length scale of the flow. 2 equation turbulence models assume a linear stress-strain relation and a length scale based on thin shear layer approximations. Therefore, these equations can be expected to perform poorly near the point of impingment where these assumptions are not valid. At locations well removed from the point of impingement, the flow approximates that of a 2D boundary layer and the 2 equation models of turbulence perform reasonable well. [copied without permission from the CFD society of Canada] http://www.cfdsc.ca/english/benchmarks/cfd95/node1.html
I believe, based on the above the although velocity will or can have some effect on the turbulation of the flow and thus the heat transfer... the equations that you are showing are incorrect... and in fact that the effects of a velocity increase are negligible when compared to the rapid decelleration and turbulation caused by the jet hitting the waterblock.
And yes... I am an engineer... even if my spelling sucks... they need a spell checker in this thing!!