Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
656261 | International Journal of Heat and Fluid Flow | 2006 | 16 Pages |
Abstract
An anisotropic low Reynolds number k–ε turbulence model has been developed and its performance compared with experimental data for fully-developed turbulent pipe flow of four different polymer solutions. Although the predictions of friction factor, mean velocity and turbulent kinetic energy show only slight improvements over those of a previous isotropic model [Cruz, D.O.A., Pinho, F.T., Resende, P.R., 2004. Modeling the new stress for improved drag reduction predictions of viscoelastic pipe flow. J. Non-Newt. Fluid Mech. 121, 127–141], the new turbulence model is capable of predicting the enhanced anisotropy of the Reynolds normal stresses that accompanies polymer drag reduction in turbulent flow.
Keywords
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Fluid Flow and Transfer Processes
Authors
P.R. Resende, M.P. Escudier, F Presti, F.T. Pinho, D.O.A. Cruz,