Reynolds-averaged modeling of turbulent flows of power-law fluids

被引:48
作者
Gavrilov, Andrey A. [1 ]
Rudyak, Valeriy Ya [2 ]
机构
[1] ICM SB RAS, Inst Thermophys SB RAS, Krasnoyarsk Branch, 50-44 Akad Gorodok, Krasnoyarsk 660036, Russia
[2] Novosibirsk State Univ Architecture & Civil Engn, 113 Leningradskaya Str, Novosibirsk 630008, Russia
基金
俄罗斯科学基金会;
关键词
Shear-thinning fluids; Power-Law fluid; Turbulence model; RANS modeling; PIPE-FLOW; NEAR-WALL; EPSILON; PREDICTIONS;
D O I
10.1016/j.jnnfm.2015.11.006
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
The paper presents a novel Reynolds-averaged turbulence model for flows of power-law fluid. The model uses the elliptic relaxation approach to capture the near-wall turbulence anisotropy. The turbulence model for Newtonians fluids is modified by introducing closed approximations of correlations between velocity and viscosity fluctuations. The approximation for non-Newtonian extra stress is derived with the assumption of smallness of molecular viscosity fluctuations. A closed model for the averaged molecular viscosity is derived which takes into account its nonlinear dependence on the shear rate. Validation of the model against the direct numerical simulation (DNS) data for power-law fluids flows in the pipe demonstrates that new model is able to predict the main features of the non-Newtonian turbulence. Mean velocity, turbulent energy and averaged molecular viscosity distributions agree well with DNS data. (c) 2015 Published by Elsevier B.V.
引用
收藏
页码:45 / 55
页数:11
相关论文
共 24 条
[1]  
[Anonymous], 2011, J APPL IND MATH
[2]   A robust k - ε - v2/k elliptic blending turbulence model applied to near-wall, separated and buoyant flows [J].
Billard, F. ;
Laurence, D. .
INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 2012, 33 (01) :45-58
[3]   VELOCITY PROFILES IN TURBULENT PIPE FLOW - NEWTONIAN AND NON-NEWTONIAN FLUIDS [J].
BOGUE, DC ;
METZNER, AB .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1963, 2 (02) :143-&
[4]   Modelling the new stress for improved drag reduction predictions of viscoelastic pipe flow [J].
Cruz, DOA ;
Pinho, FT ;
Resende, PR .
JOURNAL OF NON-NEWTONIAN FLUID MECHANICS, 2004, 121 (2-3) :127-141
[5]   Turbulent pipe flow predictions with a low Reynolds number k-ε model for drag reducing fluids [J].
Cruz, DOA ;
Pinho, FT .
JOURNAL OF NON-NEWTONIAN FLUID MECHANICS, 2003, 114 (2-3) :109-148
[6]   TURBULENT FLOW OF NON-NEWTONIAN SYSTEMS [J].
DODGE, DW ;
METZNER, AB .
AICHE JOURNAL, 1959, 5 (02) :189-204
[7]   SEPARATED FLOW COMPUTATIONS WITH THE K-EPSILON-UPSILON(2) MODEL [J].
DURBIN, PA .
AIAA JOURNAL, 1995, 33 (04) :659-664
[8]   Turbulent flow of viscoelastic shear-thinning liquids through a rectangular duct: Quantification of turbulence anisotropy [J].
Escudier, M. P. ;
Nickson, A. K. ;
Poole, R. J. .
JOURNAL OF NON-NEWTONIAN FLUID MECHANICS, 2009, 160 (01) :2-10
[9]  
Gavrilov AA, 2014, J SIB FED UNIV-MATH, V7, P46
[10]   A three dimensional exact equation for the turbulent dissipation rate of Generalised Newtonian Fluids [J].
Gori, Fabio ;
Boghi, Andrea .
INTERNATIONAL COMMUNICATIONS IN HEAT AND MASS TRANSFER, 2012, 39 (04) :477-485