Key points are not available for this paper at this time.
In this study, the role of solvent viscosity ratio () on the creeping flow characteristics of Oldroyd-B fluid over a channel-confined circular cylinder has been explored numerically. The hydrodynamic model equations have been solved by RheoTool, an open-source toolbox based on OpenFOAM, employing the finite volume method for extensive ranges of Deborah number (De = 0. 025-1. 5) and solvent viscosity ratio (= 0. 1-0. 9) for the fixed wall blockage (B = 0. 5). The present investigation has undergone extensive validation, with available literature under specific limited conditions, before obtaining detailed results for the relevant flow phenomena such as streamline, pressure and stress contour profiles, pressure coefficient (Cₚ), wall shear stress (w), normal stress (ₗₗ), first normal stress difference (N₁), and drag coefficient (C₃). The flow profiles have exhibited a distinctive behavior characterized by a loss of symmetry in the presence of pronounced viscoelastic and polymeric effects. The results for low De notably align closely with those for Newtonian fluids, and the drag coefficient (CD) remains relatively constant regardless of, as the viscoelastic influence is somewhat subdued. As De increases, the influence of viscoelasticity becomes more pronounced, while a decrease in leads to an escalation in polymeric effects; an increase in the CD value is observed as increases. Within this parameter range, the prevailing force governing the flow is the pressure drag force.
Mohanty et al. (Sat,) studied this question.