Application of wall forcing methods in a turbulent channel flow using Incompact3d

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Application of wall forcing methods in a turbulent channel flow using Incompact3d S. Khosh Aghdam Department of Mechanical Engineering - University of Sheffield

1 Flow control 2 Drag reduction 3 Maths framework 4 Simulations

Phenomenology Most of large scale engineering flows are turbulent Atmosphere Transportation (automobile, airplanes, ships, ) Blood flow in heart Aim of flow control modify the characteristics of a flow field favourably Suppression or enhancement of turbulence Dissipation of kinetic energy by turbulent flow around objects Increase of resistance to their motion Drag Component of the force experienced by a body, parallel to the direction of motion

Examples Enhancement of turbulence Mixture in combustion: quality of the fuel-air mixture determines power generation efficiency Process industry: quality of mixtures affects chemical reaction rates and purity of final products Reduction of turbulence Drag reduction techniques energy consumption issues Half of the total drag experienced by an aircraft accounts for skin-friction Aircraft industry demonstration test: Coverage of fuselage surface with riblet films ցresistance by 2% Fuel cost savings (Airbus A320) 5 10 4 L/year saving 200 million $/year

Techniques Difficulty in control design turbulence multiscale phenomenon coupling of system macroscopic size (L) & Kolmogorov scale (η) by the chaotic process of vortex stretching Two main groups active and passive Categorisation relying on energy expenditure Passive no energy added in the flow longitudinal grooves or riblets on a surface Active input of energy in the flow blowing and suction jets in opposition control[1] Based on the control loops active techniques categorisation: open-loop (predetermined) closed-loop (interactive) 1 H. Choi, P. Moin, J. Kim, Active turbulence control for drag reduction in wall-bounded flows, J. Fluid Mech.,262, 75 110, 1994

Summary Feedforward Control theory Optimal control Closed-loop Active Feedback Control techniques Open-loop Passive

Skin-friction coefficient C f = 2τ w ρ U 2 b (1) Friction velocity u τ = τ w ρ = ν y (2) wall u Reduction of velocity gradient reduction in drag Spanwise wall oscillations (active/open-loop) Steady rotating discs[2] (active/open-loop) Oscillating rotating discs (active/open-loop) Hydrophobic surfaces 2 Keefe, Method and apparatus for reducing the drag of flows over surfaces - US Patent - 1998

Functional analysis Applying control to Navier-Stokes - continuity equations (PDEs) PDEs state-space infinite-dimensional u x = 0 any f(y) solution infinite dimensional solutions space ODEs state-space dy/dt=0 solutions in p Right framework to deal with infinite-dimensional state space solutions Functional analysis Functional analysis framework: functions studied as part of normed and complete + inner product Hilbert Why Functional Analysis? Banach-L p spaces too broad for analysing PDEs solution Regularity properties not always verified in L p spaces Further assumptions higher order derivatives to ensure regularity (and boundedness) of solutions "Higher-order" spaces Sobolev energy spaces

Lyapunov stability analysis Motivation: design control laws to stabilise a specified equilibrium for the NSE NSE nonlinear nonlinear stability analysis Depart from a Lyapunov function energy of the system Choose the right norm Example: function f(t, x) (perturbed variable) with x (0, 1), within L 2 (0,1) prove that: f(t) L 2 (0,1) C 1 e C 2t f(0) L 2 (0,1) (3) C 1 1 overshoot coefficient - C 2 > 0 decay rate Find conditions for stability not necessarily nonlinear

Application Previous work: Control law in 2D channel flow based on wall-tangential actuation (Balogh et al.[3]): u(x,y=±1,t)= k u (x,±1,t) (4) y Extension to 3D channel flow carried out Link the mathematical formulation with a physical problem hydrophobic surfaces modification of no-slip condition: u u=l s y (5) wall Mathematical parameter in[3] slip-length Relevant scales for MEMS embedded sensors and actuators in the walls to measure local shear 3 A. Balogh, W. Liu, M. Krstic, Stability Enhancement by boundary control in 2D channel flow - IEEE Transactions on Automatic Control, Vol.46, No.11-2001

Application Objective stabilize a parabolic profile Boundary control laws decaying kinetic energy w.r.t time Lyapunov-based approach using Lyapunov function: Lz E(w)= w 2 L 2 (Ω) = +1 L x (u 2 + v 2 + w 2 ) dx dy dz (6) 0 1 0 translates as w(t) L 2 (Ω) C 1 e C 2(t t 0 ) w(t 0 ) L 2 (Ω) Procedure: (a) take time derivative of Eq.(6) - (b) apply control - (c) prove regularity of solutions (involving Sobolev spaces)

Benchmark L x L y L z Re p t time scheme 4π 2.0 4π/3 4200.0 2.5 10 3 AB2 L + = L Re τ U + = U Re p Re τ T + = T Re2 τ Re p Parabolic profile, constant mass flow rate, stretched wall-normal 2 Ny = 129 1.5 physical grid 1 0.5 0 0 20 40 60 80 100 120 140 computational grid

Benchmark Database of[4] used for comparison at Re τ = 180 # processors 256 512 1024 2048 runtime (s) 10348 7258 6561 6921 x,z (y=2) x,z (y=0), - u y u y 16 14 12 10 8 6 4 2 0 lower wall upper wall 0 200 400 600 t 4 R. Moser, J. Kim, N. Mansour, Direct Numerical Simulations of turbulent channel flow up to Re τ = 590,Phys. of Fluids,1999

Benchmark u y x,z walls Re τ C f,0 7.64 179.1 8.18 10 3 3 ū 15 10 5 u rms, v rms, w rms 2.5 2 1.5 1 0.5 1 10 100 y + 0 0 60 120 180 y +

Benchmark p rms 2 1.8 1.6 1.4 1.2 1 0.8 Incompact3d kmm 0.4 0.35 0.3 0.25 0.2 0.15 0.1 0.05 ω x ω y ω z ω x kmm ω y kmm ω z kmm 0.6 0 60 120 180 0 0 60 120 180 y + y +

Benchmark 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 Incompact3d kmm 0 60 120 180 y + 0.6 0.5 0.4 0.3 0.2 0.1 Profiles for uv and 0 Incompact3d kmm 0 60 120 180 uv u rms v rms y +

Spanwise wall oscillations: Overview DNS of channel flow with this forcing[5] Drag reduction Structure of forcing w=w m sin 2π T Dependent on magnitude and period of forcing Maximum DR of 40% for T + opt = 100 Experimentally[6] found DR 35% 5 Jung et. al, Physics of Fluids, 4, pp 1605 1607-1992 6 Laadhari et. al, Physics of Fluids, 6, pp 3218 3220-1994

L x L y L z n x n y n z Re τ W + m T + 4π 2.0 4π/3 256 129 128 200 27.0 125.0 DR [7] = 44.5% vs DR Incompact3d = 44.8% x,z (y=2) x,z (y=0), - u y u y 14 12 10 8 6 4 2 0 lower wall upper wall 0 750 1500 2250 7 M. Quadrio, P. Ricco, J. Fluid Mech., 521, pp 251 271-2004 t

Vorticity map at the wall 4 8 12 16 20 1.095 22.29 5 6 7 8 4.596 8.147

Steady discs rotation: overview L z L y z y x x c L x D Mean flow δ W z Active method for DR injecting vorticity Proposed as part of a patent by Keefe. Numerical study in[8] Relevant parameters (D, W), diameter and maximum tip velocity of the disc 8 P. Ricco, S. Hahn, J. Fluid Mech., 722, pp 267 290, 2013

Steady discs rotation: implementation disk_phys.dat (text file) from cpp program scr.sh disk_phys_x.dat (text file) disk_phys_z.dat (text file) rfile.f90 disk_phys_opacx.dat (binary direct open-access) disk_phys_opacz.dat (binary direct open-access) velocity components distributed on 2D Cartesian topology set as boundary conditions decomp2d_read_var interface reads disk_phys_opacx.dat and disk_phys_opacz.dat voir_visu.f90 check process with ParaView tampon_opac_x.vtr tampon_opac_z.vtr tampon_opac_sqr.vtr 0.1 0.2 0.3 2.1e-10 0.38519

Steady discs rotation: simulations L x L y L z = 6.79π 2.0 2.26π - Re p = 4200 - Nd x Nd z = 6 2 - t= 0.0025 - D + = 640 - W + = 9 KMM C f.10 3 = 8.18 BASE CASE nx ny nz= 384 129 256 C f,0.10 3 C f,0.10 3 C f.10 3 C f.10 3 Ricco-Hahn Incompact3d Ricco-Hahn Incompact3d 8.25 8.15 6.64 6.62 HIGH RESOLUTION IN x nx ny nz=480 129 224 C f,0.10 3 C f,0.10 3 C f.10 3 C f.10 3 Ricco-Hahn Incompact3d Ricco-Hahn Incompact3d 8.25 8.13 6.65 6.62 HIGH RESOLUTION IN z nx ny nz= 384 129 320 C f,0.10 3 C f,0.10 3 C f.10 3 C f.10 3 Ricco-Hahn Incompact3d Ricco-Hahn Incompact3d 8.24 8.13 6.63 6.61 HIGH RESOLUTION IN x,y,z nx ny nz=512 257 320 C f,0.10 3 C f,0.10 3 C f.10 3 C f.10 3 Ricco-Hahn Incompact3d Ricco-Hahn Incompact3d N/A 8.13 N/A 6.63

Steady discs rotation: flow visualisations u=um+ u d + ut Disc flow: u d =(u d,v d,w d )=u um Mean flow: um(y)= u with f 1 t f t i t f t i fdt and f 1 L x L z Compute 3D u 2 d + w2 in diagnostic tool+paraview d L z 0 L x fdx dz 0 0.1 0.2 0.3 2.1e-10 0.38519

Steady discs rotation: flow visualisations Isosurface representation u 2 d + w2 d = 0.09

Steady discs rotation: flow visualisations -10 0 10 20-10 20.66 Time average of the streamwise wall friction u in time window y=0 [t i h/u P ;t f h/u P ]=[750;2250] Large regions of negative wall-shear stress y

Oscillating discs Rotating discs subject to an oscillatory motion Disc tip velocity W= W m cos 2πt T Case giving optimal drag reduction xlx yly zlz nx ny nz t Re p 6.79π 2.0 3.39π 384 129 384 2.5 10 3 4200.0 Nd x Nd z D + W + T + 4 2 960 12.0 10 3 Ricco (Conf.) Incompact3d Ricco (Conf.) Incompact3d C f,0.10 3 C f,0.10 3 C f.10 3 C f.10 3 8.18 8.13 6.54 6.52

Oscillating discs Isosurface representation u 2 d + w2 d = 0.09

Hydrophobic surface: finite slip length u Studied by Min-Kim (2004) with BC forcing term: u=l s wall u, w and(u,w) can be forced but u gives optimal DR u n+1 wall = u n u wall + L n s y wall Problem: Enforce BC at each time step Generation of a thin boundary layer[10] Numerical instability Solution in[10] (1) keep the same BC for several time steps - (2) continuous update Solution adopted: compute u y at 1st time step - pass it as BC t (L s = 10 3 (s), L s = 2 10 3 (s) and L s = 10 2 (s)) compute u y at each time step - pass it as BC (L s= 10 3 (s), L s = 2 10 3 (s)and L s = 10 2 (u)) 10 C. Lee, P. Moin, J. Kim, Control of the viscous sulayer for drag redcution, J. Fluid Mech.,14, 2523 2529, 2002 y

Hydrophobic surface: preliminary results 10 9.5 9 x,z (y=0) u y 8.5 8 7.5 7 6.5 L s = 0.001 - update 1 st step L s = 0.002 - update 1 st step L s = 0.01 - update 1 st step L s = 0.001 - update for all t L s = 0.002 - update for all t 6 5.5 5 700 800 900 1000 1100 1200 t

Hydrophobic surface: statistics 3 2.5 2 no forcing L s= 0.001 L s= 0.002 L s= 0.01 0.9 0.8 0.7 0.6 u rms 1.5 v rms 0.5 0.4 1 0.3 0.5 0 0 25 50 75 100 0.2 no forcing L s= 0.001 0.1 L s= 0.002 L s= 0.01 0 0 25 50 75 100 y + y + 1.2 1 0.8 w rms 0.6 0.4 no forcing 0.2 L s= 0.001 L s= 0.002 L s= 0.01 0 0 25 50 75 100 y +

Hydrophobic surface: Summary L s 0.001 0.002 0.01 test_1 updated updated crashed test_2 constant constant constant L s u y DR DR (Kim-Min 2004) 0.001 updated 2.1% 2% 0.001 constant 2.4% 2% 0.002 updated 4.9% 5% 0.002 constant 4.9% 5% 0.01 updated NA 18% 0.01 constant 17% 18%

Summary Incompact3d efficiently dealing with various drag reduction methods High scalability allows for future control studies with larger Reynolds number