Direct Numerical Simulation of Turbulent Wall Flows at Constant - - PowerPoint PPT Presentation

direct numerical simulation of turbulent wall flows at
SMART_READER_LITE
LIVE PREVIEW

Direct Numerical Simulation of Turbulent Wall Flows at Constant - - PowerPoint PPT Presentation

14th European Turbulence Conference, Sep. 1-4 2013, Lyon, France Direct Numerical Simulation of Turbulent Wall Flows at Constant Power Input Y. Hasegawa1, B. Frohnapfel2 & M. Quadrio3 1Institute of Industrial Science, The University of


slide-1
SLIDE 1

14th European Turbulence Conference,

  • Sep. 1-4 2013, Lyon, France

Direct Numerical Simulation of Turbulent Wall Flows at Constant Power Input

  • Y. Hasegawa1, B. Frohnapfel2 & M. Quadrio3

1Institute of Industrial Science, The University of Tokyo 2Institute of Fluid Mechanics, Karlsruhe Institute of Technology

  • 3Dept. Aerospace. Eng., Polytechnic Institute of Milan
slide-2
SLIDE 2

Flow Condition in Numerical Simulation

Length: L

X X

Pump Depth: 2δ

∆P = τ

wL /δ

Pressure drop:

UB

Bulk velocity:

wall friction

 Constant Flow Rate (CFR): pressure drop (wall friction) fluctuates in time Successful Control Reduction of pressure drop  Constant Pressure Gradient (CPG): The flow rate fluctuates in time Successful Control Increase of flow rate Conventional approaches

Example: Channel flow

control,

  • bstacles,

roughness etc. Are they the only available options ?

No !

slide-3
SLIDE 3

CPI line (Constant Power Input)

Money versus Time (Frohnapfel, Hasegawa & Quadrio, JFM 2012)

(Inconvenience: time) U b

−1

Pumping Energy per Unit Mass

C f ∝U b

−1

C f ∝U b

−1/4

: laminar : turbulent

E p ∝ U b ( )

7/4

Turbulent (uncontrolled)

E p ∝U b

laminar (uncontrolled)

N A

CFR line

B

CPG line Flow control problem compromise between convenience and energy consumption

slide-4
SLIDE 4

Practical Problems

Unsteady flow in piping system Stenosis of arteries Most flow conditions in real systems should be neither CFR nor CPG !

slide-5
SLIDE 5

R

Flow rate: Q Πρεσσυρε γραδιεντ: ∆p/∆x Power input: Pp

color code corresponds to pressure gradient R CFR Q=const R CPI Pp=const R CPG ∆p/∆x=const

laminar flow in pipe w/wo orifice

slide-6
SLIDE 6

Comparison between Different Flow Conditions

Ub P ∆ ( w ∝ τ )

Pumping power ( Ub P ∝ Δ )

CFR Const. CPG Const.

Successful control

slide-7
SLIDE 7

Comparison between Different Flow Conditions

Ub P ∆ ( w ∝ τ )

Pumping power ( Ub P ∝ Δ )

CFR Const. CPG Const. CPI Const.

Successful control

 Close to real operational condition (mechanical pump, heart, ……)  Constant power input = constant dissipation = constant energy transfer rate  Optimal ratio of total power Ptotal and control power input Pc Advantage of CPI

γ = control power input total power input = P

c

P

total

= P

c

Pp + P

c

slide-8
SLIDE 8

Introduction to CPI concept

slide-9
SLIDE 9

Problem Setting

X X

Pumping power Pp

Depth: 2δ

Channel flow

Control power input Pc  Channel half depth  Fluid physical properties (kinetic viscosity: )  Total power input: Ptotal = Pp + Pc = const. Prescribed quantities

δ ν

slide-10
SLIDE 10

Velocity Scale based on Power Input

“The lower-limit of power consumption under CFR is achieved in the Stokes flow” Bewley (JFM, 2009), Fukagata et al. (Physica D, 2009)

The flow rate becomes maximum under CPI in the Stokes flow.

 Pumping power per unit wetted area  Bulk velocity in the Stokes flow

Pp = − dp dx ⎛ ⎝ ⎞ ⎠δ ⋅Ub Ub = 1 3µ − dp dx ⎛ ⎝ ⎞ ⎠δ

2 =

Ppδ 3µ

U p = P

 The upper-limit of the bulk mean velocity under CPI

Velocity scale based on the total power consumption

Pp

Stokes (laminar) flow

slide-11
SLIDE 11

Non-dimensionalization

Depth: 2δ

Channel flow

All quantities are normalized by Up = (Ptotalδ /3µ)1/2 δ

Total power input: Ptotal

Navier-Stokes & Continuity Equations:

∂ui ∂t + ∂ uiu j ( ) ∂x j = − ∂p ∂xi + 1 Re p ∂

2ui

∂x j∂x j , ∂ui ∂xi = 0

Re p = U pδ ν ≅ 6500

Evaluation of control performance

Ub /U p ≤1 ( )

Gain in flow rate

Power-based Reynolds number Total power input: P

total =

3 Re p = const. ( ) Reτ

,0 = 200

( )

slide-12
SLIDE 12

Uncontrolled flow under CPI

slide-13
SLIDE 13

Relationship between Different Reynolds Numbers in Uncontrolled Flow

slide-14
SLIDE 14

Time

Time Trace of Ub & dp/dx

slide-15
SLIDE 15

Fundamental Flow Statistics

Mean Velocity Velocity fluctuation Results in CFR, CPG & CPI converge to the identical flow state in uncontrolled flow if Reb, Re , Rep τ are adjusted properly.

slide-16
SLIDE 16

Controlled flow under CPI

Rep = 6500 (Re , 0 = 200 τ ) T+ = 125

(Spanwise wall oscillation)

x y z

Control power input Pcontrol Pumping power Ppump

P

total = Ppump + P control = const.

slide-17
SLIDE 17

Optimal Power Input

γ = P

c

P

total ~ 0.1 leads to the maximum bulk mean velocity

slide-18
SLIDE 18

Conclusions

 Constant power input (CPI) condition is proposed as a flow condition alternative to conventional CFR and CPG  close to real operational condition  power input (= energy transfer rate = dissipation) is kept constant  optimal ratio of total power input and control power input  CPI condition is first implemented in DNS of wall turbulence  Power-based velocity scale: Up  dimensionless total power input: 3/Rep  CPI simulation successfully run for the uncontrolled and controlled flows.  Uncontrolled flow under CPI is essentially same as those under CFR and CPG. In the controlled flow, the maximum Ub is obtained when is γ around 10%.

slide-19
SLIDE 19

Turbulent Intensity in Spanwise Wall Oscillation Control

: uncontrolled

urms wrms vrms

slide-20
SLIDE 20

Turbulent Intensity in Spanwise Wall Oscillation Control

: uncontrolled : CFR normalized by reference uτ

,0

slide-21
SLIDE 21

Turbulent Intensity in Spanwise Wall Oscillation Control

: uncontrolled : CFR normalized by reference uτ

,0

: CFR normalized by actual uτ

slide-22
SLIDE 22

Turbulent Intensity in Spanwise Wall Oscillation Control

: uncontrolled : CFR normalized by reference uτ

,0

: CFR normalized by actual uτ : CPG Interpretation can be changed depending on flow conditions and normalization !

slide-23
SLIDE 23

Fundamental Flow Statistics

Mean Velocity Velocity fluctuation

uncontrolled controlled

slide-24
SLIDE 24

Numerical Implementation

Advance Flow Simulation Advance Flow Simulation Calculate control Power Input Pc Calculate control Power Input Pc Calculate bulk mean velocity Calculate bulk mean velocity Calculate pressure gradient Calculate pressure gradient

Ppump

n+1 = P total − P c n

− dp dx ⎛ ⎝ ⎞ ⎠

n+1

= Ppump

n+1

Ub n → n +1

Time step:

slide-25
SLIDE 25

Energy Box

Ricco, Ottonelli, Hasegawa & Quadrio. (JFM, 2012)