Events > Applied and Numerical Analysis Seminar

A constitutive modeling of viscoelastic fluids with applications to flow in curved pipes

22/06/2001 Friday 22nd June 2001, 11:30 (Room P3.10, Mathematics Building)  More
Anne Robertson, University of Pittsburgh

There are many real fluids such as water, which the Newtonianconstitutive equation describes extremely well in almost all flowsituations. Small amounts of polymer additive can have a dramaticeffect on the behavior of these liquids. For example, B. A. Tomsstudied flows in straight pipes and discovered that in theturbulent regime small amounts of polymer additive couldsignificantly reduce the pressure drop necessary to attain a givenflow rate. These changes in behavior are attributed to theviscoelastic nature of the polymeric solution and numerousconstitutive equations have been developed to model these fluids.In contrast, in curved pipes polymer additives were foundexperimentally both to alter the relationship between pressure dropand flow rate in the laminar regime and to alter the criticalReynolds number for transition to turbulence. In this talk, we willdiscuss results for steady, fully developed flows of viscoelasticfluids in curved pipes and contrast this behavior with flows ofNewtonian fluids. Following the approach of W. R. Dean and otherauthors, we have used regular perturbation methods to study flowsof viscoelastic fluids in curved pipes. We have obtained explicitsolutions to the perturbation equations at first order for secondorder fluids and a modified Oldroyd-B fluid. In the absence ofinertial effects, flows of Newtonian fluids in curved pipes do notdisplay a secondary flow, rather a uniaxial flow exists whichdiffers only slightly from the straight pipe solution. In contrast,even in the absence of inertial effects, the class of viscoelasticfluids studied display a secondary motion (see, e.g. Thomas 1963,Bowen et al. 1991, Robertson and Muller 1996). Significantly, for acountable number of combinations of material parameters andReynolds numbers, there is a loss of uniqueness of the solution tothe perturbation equations. For other values of material parametersand Reynolds number, a solution does not even exist. There is aregion in parameter space which is free of such singularities. Thislack of existence to the perturbation equations regardless of themagnitude of the curvature ratio, implies a lack of existence of asolution which is a steady, fully developed perturbation of thestraight pipe solution. The implications of this result are underinvestigation.