Convective Transport in Channels due to the Combined Effect of Shear
and Imposed Pressure
Yogesh
Jaluria
Board
of Governors Professor & Distinguished Professor
Department
of Mechanical and Aerospace Engineering,
Rutgers
University, Piscataway, NJ 098854, USA
Email: jaluria@soe.rutgers.edu
ABSTRACT
The flow and convective heat transfer in
channels are generally due to an imposed pressure difference. Flows in mini-
and microchannels for thermal management of electronic systems and in heat
exchangers are examples of such flows. However, in many important cases, the
shear due to a moving surface may also act in conjunction with the pressure, resulting
in both aiding and opposing circumstances. Examples of such flows are seen in
lubrication and in manufacturing processes like extrusion, coating, and wire
drawing. In optical fiber drawing and coating processes, for instance, the
moving fiber imparts shear along with the imposed pressure. The transport in the
channels strongly influences the thermal processing of the material and the
final product. Similarly, cooling of optical fibers after the furnace drawing
process is another important step in the overall fiber fabrication process. The
shear is imparted by the moving fiber and inert gases like Helium and Nitrogen
are driven by pressure into the cooling channel. In extrusion processes as
well, shear and pressure driven flows arise and affect the transport mechanisms
that influence the thermal processing of the extruded material. This paper is
focused on such processes, where the flow and the convective heat transfer in
channels are induced by both shear and pressure. Of particular interest are
mini- and microchannels, though larger channels are also considered. The
transport processes at the inlet and outlet regions of the channels are of special
intertest and are discussed in detail. Experimental and numerical results are
presented to describe the flow in the channel and the resulting convective heat
transfer. The increase in pressure in channels with reducing diameter or width is
determined. This is of interest in dies and extrusion processes. It is seen that,
in several practical circumstances, high velocities and fluid viscosity result
in greater shear-induced pressures than the imposed pressure. The flow is then dominated
by the shear effects due to the moving surface. The flow in narrow channels often
develops very rapidly, resulting in largely developed flow regions. Thus, the
transport rates are relatively small over much of the flow region. Methods to
enhance the heat transfer under these circumstances by disturbing the flow are
outlined. Comparisons between experimental and numerical results show good
agreement. Therefore, the validity of the numerical models for these processes
is established. The results obtained can also be used for the design of the thermal
systems, particularly in lubrication, materials processing, and manufacturing.