A N EW A PPROACH OF Z ONAL H YBRID RANS-LES B ASED ON A T WO - - - PowerPoint PPT Presentation

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A N EW A PPROACH OF Z ONAL H YBRID RANS-LES B ASED ON A T WO - - - PowerPoint PPT Presentation

A N EW A PPROACH OF Z ONAL H YBRID RANS-LES B ASED ON A T WO - EQUATION k M ODEL [2] L ARS D AVIDSON ETMM9, Thessaloniki, 7-9 June 2012 Lars Davidson, www.tfd.chalmers.se/lada Financed by the EU project ATAAC (Advanced Turbulence


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SLIDE 1

A NEW APPROACH OF ZONAL HYBRID RANS-LES BASED ON A TWO-EQUATION k − ε MODEL [2] LARS DAVIDSON

ETMM9, Thessaloniki, 7-9 June 2012 Lars Davidson, www.tfd.chalmers.se/˜lada Financed by the EU project ATAAC (Advanced Turbulence Simulation for Aerodynamic Application Challenges) DLR, Airbus UK, Alenia, ANSYS, Beijing Tsinghua University, CFS Engineering, Chalmers, Dassault Aviation, EADS, Eurocopter Deutschland, FOI, Imperial College, IMFT, LFK, NLR, NTS, Numeca, ONERA, Rolls-Royce Deutschland, TU Berlin, TU Darmstadt, UniMAN

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SLIDE 2

PANS LOW REYNOLDS NUMBER MODEL [3]

∂k ∂t + ∂(kUj) ∂xj = ∂ ∂xj

  • ν + νt

σku ∂k ∂xj

  • + (Pk − ε)

∂ε ∂t + ∂(εUj) ∂xj = ∂ ∂xj

  • ν + νt

σεu ∂ε ∂xj

  • + Cε1Pk

ε k − C∗

ε2

ε2 k νt = Cµfµ k2 ε , C∗

ε2 = Cε1 + fk

fε (Cε2f2 − Cε1), σku ≡ σk f 2

k

fε , σεu ≡ σε f 2

k

fε Cε1, Cε2, σk, σε and Cµ same values as [1]. fε = 1. f2 and fµ read f2 =

  • 1 − exp
  • − y∗

3.1 2 1 − 0.3exp

Rt 6.5 2 fµ =

  • 1 − exp
  • − y∗

14 2 1 + 5 R3/4

t

exp

Rt 200 2 Baseline model: fk = 0.4. Range of 0.2 < fk < 0.6 is evaluated

www.tfd.chalmers.se/˜lada Zonal PANS 2 / 18

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SLIDE 3

PANS LOW REYNOLDS NUMBER MODEL [3]

∂k ∂t + ∂(kUj) ∂xj = ∂ ∂xj

  • ν + νt

σku ∂k ∂xj

  • + (Pk − ε)

∂ε ∂t + ∂(εUj) ∂xj = ∂ ∂xj

  • ν + νt

σεu ∂ε ∂xj

  • + Cε1Pk

ε k − C∗

ε2

ε2 k νt = Cµfµ k2 ε , C∗

ε2 = Cε1 + fk

fε (Cε2f2 − Cε1), σku ≡ σk f 2

k

fε , σεu ≡ σε f 2

k

fε Cε1, Cε2, σk, σε and Cµ same values as [1]. fε = 1. f2 and fµ read f2 =

  • 1 − exp
  • − y∗

3.1 2 1 − 0.3exp

Rt 6.5 2 fµ =

  • 1 − exp
  • − y∗

14 2 1 + 5 R3/4

t

exp

Rt 200 2 Baseline model: fk = 0.4. Range of 0.2 < fk < 0.6 is evaluated

www.tfd.chalmers.se/˜lada Zonal PANS 2 / 18

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SLIDE 4

PANS LOW REYNOLDS NUMBER MODEL [3]

∂k ∂t + ∂(kUj) ∂xj = ∂ ∂xj

  • ν + νt

σku ∂k ∂xj

  • + (Pk − ε)

∂ε ∂t + ∂(εUj) ∂xj = ∂ ∂xj

  • ν + νt

σεu ∂ε ∂xj

  • + Cε1Pk

ε k − C∗

ε2

ε2 k νt = Cµfµ k2 ε , C∗

ε2 = 1.5 + fk

fε (1.9 − 1.5), σku ≡ σk f 2

k

fε , σεu ≡ σε f 2

k

fε Cε1, Cε2, σk, σε and Cµ same values as [1]. fε = 1. f2 and fµ read f2 =

  • 1 − exp
  • − y∗

3.1 2 1 − 0.3exp

Rt 6.5 2 fµ =

  • 1 − exp
  • − y∗

14 2 1 + 5 R3/4

t

exp

Rt 200 2 Baseline model: fk = 0.4. Range of 0.2 < fk < 0.6 is evaluated

www.tfd.chalmers.se/˜lada Zonal PANS 2 / 18

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SLIDE 5

CHANNEL FLOW: ZONAL RANS-LES

x y ku,int, εu,int wall yint LES, fk < 1 RANS, fk = 1.0 Interface: how to treat k and ε over the interface? They should be reduced from their RANS values to suitable LES values The usual convection and diffusion across the interface is cut off, and new “interface boundary” conditions are prescribed ku,int = fkkRANS Nothing is done for ε xmax = 3.2 (64 cells), zmax = 1.6 (64 cells), y dir: 80 − 128 cells CDS in entire region

www.tfd.chalmers.se/˜lada Zonal PANS 3 / 18

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SLIDE 6

(Nx × Nz) = (64 × 64). y+

int = 500

1 100 1000 30000 5 10 15 20 25 30

y+ U+

0.05 0.1 0.15 0.2 −1 −0.8 −0.6 −0.4 −0.2

y uv+ Reτ = 4 000 Reτ = 8 000 Reτ = 16 000; Reτ = 32 000.

www.tfd.chalmers.se/˜lada Zonal PANS 4 / 18

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SLIDE 7

INTERFACE LOCATION. Reτ = 8 000.

1 100 1000 8000 5 10 15 20 25 30

y+ U+

500 1000 1500 2000 −1 −0.8 −0.6 −0.4 −0.2

y+ uv+ y+ = 130 y+ = 500 y+ = 980

www.tfd.chalmers.se/˜lada Zonal PANS 5 / 18

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SLIDE 8

EFFECT OF fk. Reτ = 16 000. y+

int = 500

1 100 1000 10000 5 10 15 20 25 30

y+ U+

0.05 0.1 0.15 0.2 −1 −0.8 −0.6 −0.4 −0.2

y uv+ fk = 0.2 fk = 0.3 fk = 0.5 fk = 0.6

www.tfd.chalmers.se/˜lada Zonal PANS 6 / 18

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SLIDE 9

EFFECT OF RESOLUTION: VELOCITY

1 100 1000 30000 5 10 15 20 25 30

(Nx × Nz) = (32 × 32) y+ U+

1 100 1000 30000 5 10 15 20 25 30

(Nx × Nz) = (128 × 128) y+ U+ Reτ = 4 000 Reτ = 8 000 Reτ = 16 000; Reτ = 32 000.

www.tfd.chalmers.se/˜lada Zonal PANS 7 / 18

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SLIDE 10

EFFECT OF RESOLUTION: RESOLVED SHEAR STRESS

0.05 0.1 0.15 0.2 −1 −0.8 −0.6 −0.4 −0.2

(Nx × Nz) = (32 × 32) y uv+

0.05 0.1 0.15 0.2 −1 −0.8 −0.6 −0.4 −0.2

(Nx × Nz) = (128 × 128) y uv+ Reτ = 4 000 Reτ = 8 000 Reτ = 16 000; Reτ = 32 000.

www.tfd.chalmers.se/˜lada Zonal PANS 8 / 18

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SLIDE 11

EFFECT OF RESOLUTION: TURBULENT VISCOSITY

0.05 0.1 0.15 0.2 0.25 0.3 0.005 0.01 0.015

Reτ = 4000 νt/(uτδ)

0.05 0.1 0.15 0.2 0.25 0.3 0.005 0.01 0.015

Reτ = 8000

0.05 0.1 0.15 0.2 0.25 0.3 0.005 0.01 0.015

Reτ = 16 000 y νt/(uτδ)

0.05 0.1 0.15 0.2 0.25 0.3 0.005 0.01 0.015

Reτ = 32 000 y (Nx × Nz) = 64 × 64 32 × 32 128 × 128

www.tfd.chalmers.se/˜lada Zonal PANS 9 / 18

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SLIDE 12

EFFECT OF RESOLUTION: TURBULENT VISCOSITY

0.05 0.1 0.15 0.2 0.25 0.3 0.005 0.01 0.015

Reτ = 4000 νt/(uτδ)

0.05 0.1 0.15 0.2 0.25 0.3 0.005 0.01 0.015

Reτ = 8000

0.05 0.1 0.15 0.2 0.25 0.3 0.005 0.01 0.015

Reτ = 16 000 y νt/(uτδ)

0.05 0.1 0.15 0.2 0.25 0.3 0.005 0.01 0.015

Reτ = 32 000 y (Nx × Nz) = 64 × 64 32 × 32 128 × 128

G r i d i n d e p e n d e n t t u r b u l e n t v i s c

  • s

i t y !

www.tfd.chalmers.se/˜lada Zonal PANS 9 / 18

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SLIDE 13

SGS MODELS BASED ON GRID SIZE

When the grid is refined, νt gets smaller

www.tfd.chalmers.se/˜lada Zonal PANS 10 / 18

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SLIDE 14

SGS MODELS BASED ON GRID SIZE

When the grid is refined, νt gets smaller E εsgs κ Pk,res κc

www.tfd.chalmers.se/˜lada Zonal PANS 10 / 18

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SLIDE 15

SGS MODELS BASED ON GRID SIZE

When the grid is refined, νt gets smaller E εsgs,∆ εsgs,0.5∆ κ Pk,res κc 2κc

www.tfd.chalmers.se/˜lada Zonal PANS 10 / 18

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SLIDE 16

SGS MODELS BASED ON GRID SIZE

When the grid is refined, νt gets smaller E εsgs,∆ εsgs,0.5∆ κ Pk,res κc 2κc εsgs,∆ = εsgs,0.5∆ εsgs = 2νt¯ sij¯ sij − τ12,t∂¯ u ∂y Grid refinement ⇒ must be accompanied with larger ¯ sij¯ sij ⇒ ¯ sij¯ sij must take place at higher wavenumbers if not ⇒ grid dependent

www.tfd.chalmers.se/˜lada Zonal PANS 10 / 18

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SLIDE 17

POWER DENSITY SPECTRA OF ν0.5

t

∂ ¯ w′ ∂z

20 40 60 80 100 0.005 0.01 0.015 0.02

E

  • νt (∂ ¯

w′/∂z)2 κz One-eq ksgs model

20 40 60 80 100 0.005 0.01 0.015 0.02 0.025 0.03

κz Zonal PANS (Nx × Nz) = 64 × 64 32 × 32 128 × 128

www.tfd.chalmers.se/˜lada Zonal PANS 11 / 18

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SLIDE 18

SGS DISSIPATION VS. WAVENUMBER

Energy spectra of the SGS dissipation show that the peak takes place at surprisingly low wavenumber (length scale corresponding to 10 cells or more). κc κ E(κ) εsgs

www.tfd.chalmers.se/˜lada Zonal PANS 12 / 18

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SLIDE 19

SGS DISSIPATION VS. WAVENUMBER

Energy spectra of the SGS dissipation show that the peak takes place at surprisingly low wavenumber (length scale corresponding to 10 cells or more). κc κ E(κ) εsgs εsgs,κ

www.tfd.chalmers.se/˜lada Zonal PANS 12 / 18

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SLIDE 20

SGS DISSIPATION, Reτ = 8000

SGS dissipation in the ¯ u′

i ¯

u′

i/2 eq, εsgs = 2νt¯

sij¯ sij − τ12,t∂¯ u ∂y

0.1 0.15 0.2 0.25 0.3 5 10 15

y εsgs One-eq ksgs model

0.1 0.15 0.2 0.25 0.3 5 10 15

y εsgs Zonal PANS (Nx × Nz) = 64 × 64 32 × 32 128 × 128

www.tfd.chalmers.se/˜lada Zonal PANS 13 / 18

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SLIDE 21

LOCAL EQUILIBRIUM. Reτ = 4000, Nx × Nz = 64 × 64.

0.1 0.2 0.3 0.4 0.5 0.6 0.1 0.2 0.3 0.4 0.1 0.2 0.3 0.4 0.5 0.6 2E−3 4E−3 0.1 0.2 0.3 0.4 0.5 0.6 2E−3 4E−3

y k equation

0.1 0.2 0.3 0.4 0.5 0.6 0.01 0.02 0.03 0.1 0.2 0.3 0.4 0.5 0.6 2E−4 4E−4 0.1 0.2 0.3 0.4 0.5 0.6 2E−4 4E−4

ε equation y Pk+ ε+ Cε1Pk/ε+ Cε2ε2/k+ Left vertical axes: URANS region; right vertical axes: LES region.

www.tfd.chalmers.se/˜lada Zonal PANS 14 / 18

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SLIDE 22

LOCAL EQUILIBRIUM IN ε EQUATION.

How can both the k eq. and ε be in local equilibrium??

www.tfd.chalmers.se/˜lada Zonal PANS 15 / 18

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SLIDE 23

LOCAL EQUILIBRIUM IN ε EQUATION.

How can both the k eq. and ε be in local equilibrium?? If Pk = ε

www.tfd.chalmers.se/˜lada Zonal PANS 15 / 18

slide-24
SLIDE 24

LOCAL EQUILIBRIUM IN ε EQUATION.

How can both the k eq. and ε be in local equilibrium?? If Pk = ε then C1 ε kPk=C∗

2

ε2 k , because C1 = C∗

2

www.tfd.chalmers.se/˜lada Zonal PANS 15 / 18

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SLIDE 25

LOCAL EQUILIBRIUM IN ε EQUATION.

How can both the k eq. and ε be in local equilibrium?? If Pk = ε then C1 ε kPk=C∗

2

ε2 k , because C1 = C∗

2

However, the figure on previous slide shows C1 ε k Pk

  • = C∗

2

ε2 k

  • www.tfd.chalmers.se/˜lada

Zonal PANS 15 / 18

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SLIDE 26

LOCAL EQUILIBRIUM IN ε EQUATION.

How can both the k eq. and ε be in local equilibrium?? If Pk = ε then C1 ε kPk=C∗

2

ε2 k , because C1 = C∗

2

However, the figure on previous slide shows C1 ε k Pk

  • = C∗

2

ε2 k

  • Answer: when time-averaging ab = ab

www.tfd.chalmers.se/˜lada Zonal PANS 15 / 18

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SLIDE 27

LOCAL EQUILIBRIUM IN ε EQUATION.

The answer is because of time averaging (ab < ab, (see below)

0.1 0.2 0.3 0.4 0.5 0.6 1 1.05 1.1 1.15 1.2

y εPk/k εPk/k ε2/k ε2/k

www.tfd.chalmers.se/˜lada Zonal PANS 16 / 18

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SLIDE 28

RESOLVED AND MODELLED TURBULENT KINETIC ENERGY.

0.1 0.2 0.3 0.4 1 2 3 4 5 6 7 8

Resolved y kres

0.1 0.2 0.3 0.4 1 2 3 4 5 6 7 8

Modelled: bottom; total: top y k, kres + k Reτ = 4 000 Reτ = 8 000 Reτ = 16 000; Reτ = 32 000.

www.tfd.chalmers.se/˜lada Zonal PANS 17 / 18

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SLIDE 29

CONCLUDING REMARKS

LRN PANS works well as zonal LES-RANS model for very high Reτ (> 32 000) The model gives grid independent results The location of the interface is not important (it should not be too close to the wall) Values of 0.2 < fk < 0.5 have little impact on the results

www.tfd.chalmers.se/˜lada Zonal PANS 18 / 18

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SLIDE 30

[1] ABE, K., KONDOH, T., AND NAGANO, Y. A new turbulence model for predicting fluid flow and heat transfer in separating and reattaching flows - 1. Flow field calculations.

  • Int. J. Heat Mass Transfer 37 (1994), 139–151.

[2] DAVIDSON, L. A new approach of zonal hybrid RANS-LES based on a two-equation k − ε model. In ETMM9: International ERCOFTAC Symposium on Turbulence Modelling and Measurements (Thessaloniki, Greece, 2012). [3] MA, J., PENG, S.-H., DAVIDSON, L., AND WANG, F. A low Reynolds number variant of Partially-Averaged Navier-Stokes model for turbulence. International Journal of Heat and Fluid Flow 32 (2011), 652–669.

www.tfd.chalmers.se/˜lada Zonal PANS 18 / 18