Turbulent duct flow with polymers

被引:34
作者
Shahmardi, Armin [1 ,2 ]
Zade, Sagar [1 ,2 ]
Ardekani, Mehdi N. [1 ,2 ]
Poole, Rob J. [3 ]
Lundell, Fredrik [1 ,2 ]
Rosti, Marco E. [1 ,2 ]
Brandt, Luca [1 ,2 ]
机构
[1] KTH Mech, Linne Flow Ctr, SE-10044 Stockholm, Sweden
[2] KTH Mech, SeRC Swedish & Sci Res Ctr, SE-10044 Stockholm, Sweden
[3] Univ Liverpool, Dept Engn, Brownlow St, Liverpool L69 3GH, Merseyside, England
基金
英国工程与自然科学研究理事会; 欧洲研究理事会; 瑞典研究理事会;
关键词
drag reduction; polymers; turbulence simulation; DIRECT NUMERICAL-SIMULATION; MAXIMUM DRAG REDUCTION; CHANNEL FLOW; PIPE-FLOW; REYNOLDS-NUMBER; WALL TURBULENCE; SECONDARY FLOW; STRESS; FLUID; PREDICTIONS;
D O I
10.1017/jfm.2018.858
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
We have performed direct numerical simulation of the turbulent flow of a polymer solution in a square duct, with the FENE-P model used to simulate the presence of polymers. First, a simulation at a fixed moderate Reynolds number is performed and its results compared with those of a Newtonian fluid to understand the mechanism of drag reduction and how the secondary motion, typical of the turbulent flow in non-axisymmetric ducts, is affected by polymer additives. Our study shows that the Prandtl's secondary flow is modified by the polymers: the circulation of the streamwise main vortices increases and the location of the maximum vorticity moves towards the centre of the duct. In-plane fluctuations are reduced while the streamwise ones are enhanced in the centre of the duct and dumped in the corners due to a substantial modification of the quasi-streamwise vortices and the associated near-wall low- and high-speed streaks; these grow in size and depart from the walls, their streamwise coherence increasing. Finally, we investigated the effect of the parameters defining the viscoelastic behaviour of the flow and found that the Weissenberg number strongly influences the flow, with the cross-stream vortical structures growing in size and the in-plane velocity fluctuations reducing for increasing flow elasticity.
引用
收藏
页码:1057 / 1083
页数:27
相关论文
共 67 条
[1]   Effect of a high-resolution differencing scheme on finite-volume predictions of viscoelastic flows [J].
Alves, MA ;
Pinho, FT ;
Oliveira, PJ .
JOURNAL OF NON-NEWTONIAN FLUID MECHANICS, 2000, 93 (2-3) :287-314
[2]   Streak instability in viscoelastic Couette flow [J].
Biancofiore, L. ;
Brandt, L. ;
Zaki, T. A. .
PHYSICAL REVIEW FLUIDS, 2017, 2 (04)
[3]   The influence of wall permeability on turbulent channel flow [J].
Breugem, W. P. ;
Boersma, B. J. ;
Uittenbogaard, R. E. .
JOURNAL OF FLUID MECHANICS, 2006, 562 :35-72
[4]   THE PRODUCTION AND DIFFUSION OF VORTICITY IN DUCT FLOW [J].
BRUNDRETT, E ;
BAINES, WD .
JOURNAL OF FLUID MECHANICS, 1964, 19 (03) :375-394
[5]  
Cho Y., 1982, Advances in Heat Transfer, V15, P59, DOI DOI 10.1016/S0065-2717(08)70173-4
[6]   DIRECT NUMERICAL-SIMULATION OF TURBULENT-FLOW OVER RIBLETS [J].
CHOI, H ;
MOIN, P ;
KIM, J .
JOURNAL OF FLUID MECHANICS, 1993, 255 :503-539
[7]   DNS of wall turbulence: dilute polymers and self-sustaining mechanisms [J].
De Angelis, E ;
Casciola, CM ;
Piva, R .
COMPUTERS & FLUIDS, 2002, 31 (4-7) :495-507
[8]   Elastoviscoplastic flows in porous media [J].
De Vita, F. ;
Rosti, M. E. ;
Izbassarov, D. ;
Duffo, L. ;
Tammisola, O. ;
Hormozi, S. ;
Brandt, L. .
JOURNAL OF NON-NEWTONIAN FLUID MECHANICS, 2018, 258 :10-21
[9]  
Dealy J.M., 2010, Rheol. Bull, V79, P14
[10]   Drag reduction by polymer additives in a turbulent pipe flow: Numerical and laboratory experiments [J].
DenToonder, JMJ ;
Hulsen, MA ;
Kuiken, GDC ;
Nieuwstadt, FTM .
JOURNAL OF FLUID MECHANICS, 1997, 337 :193-231