Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
7054517 | International Journal of Heat and Mass Transfer | 2018 | 16 Pages |
Abstract
Steady-state laminar mixed convection of Bingham fluids in cylindrical enclosures with a rotating top cover has been numerically analysed for the configuration where the bottom cover is kept at a higher temperature than the rotating top cover. The numerical investigations have been carried out based on steady-state axisymmetric incompressible flow simulations for a range of different values Reynolds, Richardson, and Prandtl number given by 500⩽Re⩽3000, 0⩽Ri⩽1 and 10⩽Pr⩽500 respectively. The aspect ratio (i.e. height: radiusâ¯=â¯ARâ¯=â¯H/R) of the cylindrical container is considered to be unity (i.e. ARâ¯=â¯H/Râ¯=â¯1). The mean Nusselt number Nuâ¾ has been found to decrease sharply with increasing Bn owing to flow resistance arising from yield stress, but subsequently Nuâ¾ asymptotically approaches a value of unity, which is indicative of a conduction-driven transport. In addition, the mean Nusselt number Nuâ¾ has been found to increase with increasing Reynolds number due to the strengthening of advective transport. However, the mean Nusselt number Nuâ¾ exhibits a non-monotonic trend (i.e. increases with increasing Ri for small values of Richardson number before showing a weak decreasing trend) with increasing Ri for Newtonian fluid (i.e. Bn=0), whereas Nuâ¾ increases with increasing Ri for small values of Richardson number before becoming a weak function of Ri for Bingham fluids. A step change in the mean Nusselt number has also been observed with an increase in Richardson number for some Bingham number values due to a change in flow pattern. The influences of Prandtl, Reynolds, Richardson, and Bingham numbers on the mean Nusselt number have been explained in detail based on both physical and scaling arguments. The simulation data and scaling relations have been utilised to propose a correlation for the mean Nusselt number, which has been shown to capture the numerical findings satisfactorily for the parameter range considered here.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Fluid Flow and Transfer Processes
Authors
Osman Turan, Nilanjan Chakraborty,