A viscoelastic k-ε-v2¯-f turbulent flow model valid up to the maximum drag reduction limit

Abstract A tensorially consistent near-wall four equation model is developed to model turbulent flow of dilute polymer solutions. The model is validated up to the maximum drag reduction limit, by utilizing the data obtained from direct numerical simulations using the finitely extensible nonlinear elastic-Peterlin (FENE-P) constitutive model. Eight sets of direct numerical simulation (DNS) data are used to analyze budgets of relevant physical quantities, such as the nonlinear terms in the FENE-P constitutive equation, the turbulent kinetic energy, the wall normal Reynolds stress and dissipation transport. Closures were developed in the framework of the k - e - v 2 ¯ - f model for the viscoelastic stress work, the viscoelastic destruction of the rate of dissipation, the viscoelastic turbulent viscosity, and the interactions between the fluctuating components of the conformation tensor and of the velocity gradient tensor terms. Predicted polymer stress, velocity profiles and turbulent flow characteristics are all in good agreement with the literature, from which six independent DNS data sets were used covering a wide range of rheological and flow parameters, including high Reynolds number flows, and showing significant improvements over the corresponding predictions of other existing models.

[1]  van den Bhaa Ben Brule,et al.  Turbulent channel flow near maximum drag reduction: simulations, experiments and mechanisms , 2003, Journal of Fluid Mechanics.

[2]  P. R. Resende,et al.  Numerical predictions and measurements of Reynolds normal stresses in turbulent pipe flow of polymers , 2006 .

[3]  P. G. de Gennes,et al.  A Cascade Theory of Drag Reduction , 1986 .

[4]  T. Gatski,et al.  Analysis of Polymer Drag Reduction Mechanisms from Energy Budgets , 2013 .

[5]  Kyoungyoun Kim,et al.  A FENE-P k e turbulence model for low and intermediate regimes of polymer-induced drag reduction , 2011 .

[6]  A. G. Fabula,et al.  THE EFFECT OF ADDITIVES ON FLUID FRICTION , 1964 .

[7]  S. Balachandar,et al.  Effects of polymer stresses on eddy structures in drag-reduced turbulent channel flow , 2006, Journal of Fluid Mechanics.

[8]  Gianluca Iaccarino,et al.  Reynolds-averaged modeling of polymer drag reduction in turbulent flows , 2010 .

[9]  Brian J. Edwards,et al.  Thermodynamics of flowing systems : with internal microstructure , 1994 .

[10]  Arne V. Johansson,et al.  Pressure fluctuation in high-Reynolds-number turbulent boundary layer: results from experiments and DNS , 2012 .

[11]  Chang Feng Li,et al.  Influence of rheological parameters on polymer induced turbulent drag reduction , 2006 .

[12]  Li Xi,et al.  Active and hibernating turbulence in minimal channel flow of newtonian and polymeric fluids. , 2009, Physical review letters.

[13]  David T. Walker,et al.  Reynolds Stress Modeling for Drag Reducing Viscoelastic Flows , 2002 .

[14]  Parviz Moin,et al.  On the coherent drag-reducing and turbulence-enhancing behaviour of polymers in wall flows , 2004, Journal of Fluid Mechanics.

[15]  P. J. Dotson,et al.  Polymer solution rheology based on a finitely extensible bead—spring chain model , 1980 .

[16]  Fernando T. Pinho,et al.  Corrigendum to “A low Reynolds number turbulence closure for viscoelastic fluids” [Journal of Non-Newtonian Fluid Mechanics 154 (2008) 89–108] , 2012 .

[17]  R. Handler,et al.  Budgets of Reynolds stress, kinetic energy and streamwise enstrophy in viscoelastic turbulent channel flow , 2001 .

[18]  Robert A. Handler,et al.  Viscoelastic effects on higher order statistics and on coherent structures in turbulent channel flow , 2005 .

[19]  Robert A. Handler,et al.  Direct numerical simulation of the turbulent channel flow of a polymer solution , 1997 .

[20]  David G. Bogard,et al.  Wall-layer structure and drag reduction , 1985, Journal of Fluid Mechanics.

[21]  V. K. Gupta,et al.  Turbulent channel flow of dilute polymeric solutions: Drag reduction scaling and an eddy viscosity model , 2006 .

[22]  P. R. Resende,et al.  A Reynolds stress model for turbulent flows of viscoelastic fluids , 2013 .

[23]  Robert C. Armstrong,et al.  Dynamics of polymeric liquids: Kinetic theory , 1987 .

[24]  Thomas B. Gatski,et al.  SOME DYNAMICAL FEATURES OF THE TURBULENT FLOW OF A VISCOELASTIC FLUID FOR REDUCED DRAG , 2012, Proceeding of Seventh International Symposium on Turbulence and Shear Flow Phenomena.

[25]  F. Pinho A GNF framework for turbulent flow models of drag reducing fluids and proposal for a k–ε type closure , 2003 .

[26]  W. Squire,et al.  The effect of polymer additives on transition in pipe flow , 1968 .

[27]  P. S. Virk An elastic sublayer model for drag reduction by dilute solutions of linear macromolecules , 1971, Journal of Fluid Mechanics.

[28]  Parviz Moin,et al.  Direct numerical simulation of polymer-induced drag reduction in turbulent boundary layer flow , 2005 .

[29]  P. Durbin Near-wall turbulence closure modeling without “damping functions” , 1991, Theoretical and Computational Fluid Dynamics.

[30]  W. Giles,et al.  Stability of Dilute Viscoelastic Flows , 1967, Nature.

[31]  John L. Lumley,et al.  Drag reduction in turbulent flow by polymer additives , 1973 .

[32]  Fernando T. Pinho,et al.  A low Reynolds number turbulence closure for viscoelastic fluids , 2008 .

[33]  R. Adrian,et al.  Dynamics of hairpin vortices and polymer-induced turbulent drag reduction. , 2008, Physical review letters.

[34]  John L. Lumley,et al.  Drag Reduction by Additives , 1969 .

[35]  J. Hoyt A Freeman Scholar Lecture: The Effect of Additives on Fluid Friction , 1972 .

[36]  P. S. Virk Drag reduction fundamentals , 1975 .

[37]  W. G. Tiederman,et al.  Spatial structure of the viscous sublayer in drag‐reducing channel flows , 1975 .