The Influence of Polymer Additives On Turbulent Energy Distribution In Fully-Developed Channel Flows

Monday, November 8, 2010
Hall 1 (Salt Palace Convention Center)
Andre Benard1, Ryan J. Dowty2, Satish Muthu2 and Charles A. Petty2, (1)Mechanical Engineering, Michigan State University, East Lansing, MI, (2)Chemical Engineering and Materials Science, Michigan State University, East Lansing, MI

The mean velocity and pressure fields for turbulent flows of constant property viscoelastic fluids are governed by the continuity equation and the Reynolds averaged Cauchy (RAC-) equation. The RAC-equation is an exact, unclosed equation for the mean velocity. Closure requires a model for the mean Cauchy stress and for the Reynolds stress. In this paper, a recently developed closure for the normalized Reynolds (NR-) stress for turbulent flows of viscous fluids (Koppula, et al., 2009) is extended to turbulent flows of viscoelastic fluids (Virk, 1975; Lyons and Petty, 1985; Brostow, 2008; White and Mungal, 2008). The results are used to predict the influence of polymer additives on the NR-stress in fully-developed channel flows.

References: Brostow, W., 2008, “Drag Reduction in Flow: Review of Applications, Mechanism and Prediction”, Journal of Industrial and Engineering Chemistry, 14(4), 409-416. Koppula, K.S., A. Bénard, and C. A. Petty, 2009, “Realizable Algebraic Reynolds Stress Closure”, Chemical Engineering Science, 64, 4611-4624. Lyons, S. and C. A. Petty, 1985, “Predictions of Turbulent Drag Reduction for a Linear Viscoelastic Fluid”, p. 310 in The Influence of Polymer Additives on Velocity and Temperature Fields, Editor: B. Gampert, 1984 IUTAM Symposium, Essen, Germany, Springer-Verlag. Virk, P. S., 1975, “Drag Reduction Fundamentals”, AIChE Journal, 21(4), 625-656. White, C. M. and M.G. Mungal, 2008, “Mechanics and Prediction of Turbulent Drag Reduction with Polymer Additives”, Annual Review of Fluid Mechanics, 40, 235-256.


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See more of this Session: Poster Session: Fluid Mechanics
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