r. j. poole and m. p. escudier dept. engineering, mechanical engineering, university of liverpool

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R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool Liverpool L69 3GH, UK, [email protected],[email protected] 3D FLOW OF VISCOELASTIC FLUIDS OVER A 3D FLOW OF VISCOELASTIC FLUIDS OVER A BACKWARD-FACING STEP PRECEDED BY A GRADUAL BACKWARD-FACING STEP PRECEDED BY A GRADUAL CONTRACTION CONTRACTION A. Afonso Centro de Estudos de Fenómenos de Transporte, DEMEGI Faculdade de Engenharia, Universidade do Porto, Portugal, [email protected] F. T. Pinho Centro de Estudos de Fenómenos de Transporte, Dep. Eng. Mecânica Escola de Engenharia, Universidade do Minho, Portugal, [email protected] AERC 2005 22 nd to 24 th April 2005 Grenoble, France

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3D FLOW OF VISCOELASTIC FLUIDS OVER A BACKWARD-FACING STEP PRECEDED BY A GRADUAL CONTRACTION. A. Afonso Centro de Estudos de Fenómenos de Transporte, DEMEGI Faculdade de Engenharia, Universidade do Porto, Portugal, [email protected]. F. T. Pinho - PowerPoint PPT Presentation

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Page 1: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

R. J. Poole and M. P. EscudierDept. Engineering, Mechanical Engineering, University of LiverpoolLiverpool L69 3GH, UK, [email protected],[email protected]

3D FLOW OF VISCOELASTIC FLUIDS OVER A 3D FLOW OF VISCOELASTIC FLUIDS OVER A

BACKWARD-FACING STEP PRECEDED BY A BACKWARD-FACING STEP PRECEDED BY A

GRADUAL CONTRACTIONGRADUAL CONTRACTION

A. AfonsoCentro de Estudos de Fenómenos de Transporte, DEMEGI Faculdade de Engenharia, Universidade do Porto, Portugal, [email protected]

F. T. PinhoCentro de Estudos de Fenómenos de Transporte, Dep. Eng. MecânicaEscola de Engenharia, Universidade do Minho, Portugal, [email protected]

AERC 200522nd to 24th April 2005 Grenoble, France

Page 2: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Flow geometry

Experiments of Poole et al (2004) with solutions of PAA

Area ratio R = d/D = 0.7

Upstream spanwise velocity profiles (x-z plane) at x/h=-8.33 and 0

d = 28mm, h = 6mm,

D = 40mm, w = 80mm

Inlet duct: 120 DH long

(area ratio > 2/3 double backward-facing step )

Aspect ratios A1 = w/h = 13.3

A2 = w/d= 2.86

Page 3: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Experimental and numerical findings

Figure : Spanwise variation of mean streamwise velocity ( U/UB ) profiles for 0.1% PAA

z / w

U/UB

0 0.25 0.5 0.75 10

0.2

0.4

0.6

0.8

1

1.2

1.4

1.6

0

0.2

0.4

0.6

0.8

1

1.2

1.4

1.6

NewtonianCarreau-YasudaPTT

x / h = 0

0.1% PAA

x / h = -8.33

0.1% PAA Re 120

Cat’s ears

Spanwise variation at y/D=0.5GNF

PTT(N2=0)

Page 4: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Experimental and numerical findings 3

0.1% PAA Re 120Downstream

Figure : Mean streamwise velocity ( U/UB ) profiles for 0.1% PAA

y/D

0

0.05

0.1

0.15

0.2

0.25

0.3

0.35

0

0.05

0.1

0.15

0.2

0.25

0.3

0.35

PTTx/h0 1 2 3 4

1

U = 0

XR = 2.3

Newtonian Carreau-Yasuda

Page 5: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Objective

Cat’s ears: Why?

Shear-thinning:No

Elasticity - : No Ψ1

Qualitative calculation with PTT: parametric investigation

Effect of

Effect of De

Effect of

Effect of Re

Ψ2

ηe

Individual and combined effects

Page 6: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Governing equations

∂∂tJρui( ) +

∂ξ lρβ lj %u jui( ) = −β li

∂p

∂ξ l+

∂ξ lβ lj %τ ij , p + β ljτ ij ,s( ) + +Jρgi

1) Mass

2) Momentum

3) Constitutive equation

1+λε

η pτ kk,p

⎝ ⎜ ⎜

⎠ ⎟ ⎟τ ij,p + λ

∂τ ij,p∂t

+∂ ukτ ij,p( )

∂xk

⎝ ⎜ ⎜

⎠ ⎟ ⎟=η p

∂ui∂x j

+∂u j∂xi

⎝ ⎜ ⎜

⎠ ⎟ ⎟+ λ τ jk,p

∂ui∂xk

+ τ ik,p∂u j∂xk

⎝ ⎜

⎠ ⎟−

λξ2τ jk,p

∂ui∂xk

+∂uk∂xi

⎝ ⎜

⎠ ⎟+ τ ik,p

∂u j∂xk

+∂uk∂x j

⎝ ⎜ ⎜

⎠ ⎟ ⎟

⎝ ⎜ ⎜

⎠ ⎟ ⎟

Full PTT (linear stress coefficient)

τ ij = 2η sDij + τ ij , p

Newtonian solvent

Page 7: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Numerical method: brief description

2) Structured, colocated and non-orthogonal meshes

3) Momentum (ui)

∂∂t

Jρui( )+∂

∂ξlρβlj ˜ u j ˆ u i( )−

∂∂ξl

ηp

Jβljβlj

∂ui∂ξl

⎝ ⎜ ⎜

⎠ ⎟ ⎟ −

∂ βljτij,s( )

∂ξl=−βli

∂p∂ξl

+∂

∂ξlβlj˜ τ ij( )+Jρgi −

∂∂ξl

ηp

Jβljβlj

∂ui∂ξl

⎝ ⎜ ⎜

⎠ ⎟ ⎟

solvent polymer

1) Finite volume method (Oliveira et al,1998; Oliveira & Pinho, 1999)

4) Discretization (formally 2nd order)Diffusive terms: central differences (CDS)Advective terms: CUBISTA (deferred correction)

(Alves et al, 2000, 2003)

5) Special formulations for cell-face velocities and stresses

Page 8: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Computational domain and mesh

5 m (62 DH)

120 h

20 cells

30 cells

102 000 total cells1 020 000 DF

Page 9: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Inlet flow

x/h=-16

ξ =0.001 ξ =0.2

ε =0.05,λ = 0.1 s,η p = 0.5 Pa.s,η s = 0.05 Pa.s

Page 10: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Non-dimensional numbers

Re'= ρUbhηs+ηp( )

Reynolds number

De=Ubλp

hDeborah number

Re=ρUbhμc

&γC =Ubh

with and

ε

ξ

Extensional parameter

Slip parameter

Bulk velocity at contraction exit

Page 11: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Effect of ξ: 1

Re '=5.14

kitten’s ears

Absence of kitten’s ears

Several values of ε

ε =0.15

Page 12: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Effect of ξ: 2

Re '=5.14

kitten’s ears:high De, high ξ, low ε

Page 13: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Effect of ξ: 3

Re '=5.14x h=−8.0;−4.0;−2.06;−0.1

kitten’s ears

x/h=-8

x/h=-4

x/h=-2.06

x/h=-0.1

Effect ofinertia

Page 14: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Effect of εRe '=5.14 ξ =0.2

Closed symbols: kitten’s ears

x/h=-8

x/h=-4

x/h=-2.06

x/h=-0.1

(a) (b)

Effect of De (next slide)

Page 15: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Effect of De

Re '=5.14 ξ =0.2

ε =0.025ε =0.1

DeDe

Page 16: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Effect of Re’: 1

ξ =0.2 ε =0.005De=19.6 De=39.2

QuickTime™ and aBMP decompressor

are needed to see this picture.

QuickTime™ and aBMP decompressor

are needed to see this picture.

Re=0.6 Re’=0.48 Re=0.6 Re’=0.43

Page 17: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Effect of Re’: 2

ξ =0.2 ε =0.005De=19.6 De=39.2

Re=1.7 Re’=1.4 Re=1.7 Re’=1.3

QuickTime™ and aBMP decompressor

are needed to see this picture.

QuickTime™ and aBMP decompressor

are needed to see this picture.

Page 18: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Effect of Re’: 3

ξ =0.2 ε =0.005De=19.6 De=39.2

Re=3.4 Re’=2.8 Re=3.4 Re’=2.6

QuickTime™ and aBMP decompressor

are needed to see this picture.

QuickTime™ and aBMP decompressor

are needed to see this picture.

Page 19: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Effect of Re’: 4

ξ =0.2 ε =0.005De=19.6 De=39.2

Re=6.3 Re’=5.2 Re=6.3 Re’=4.7

QuickTime™ and aBMP decompressor

are needed to see this picture.

QuickTime™ and aBMP decompressor

are needed to see this picture.

Page 20: R. J. Poole and M. P. Escudier Dept. Engineering, Mechanical Engineering, University of Liverpool

3D Viscoelastic flow in smooth contractions European Congress on Rheology

AERC 2005

Conclusions

•Cat’s ears are qualitatively predicted by PTT (kitten’s ears)

•N2≠ 0 (essential)— high ξ

•Low ε

•High De

•Intermediate Re

•Sometimes enhanced peaks observed at corners

•Low Re: very slim profiles at contraction exit, no peaks

•High Re: flat profiles at contracton exit, no peaks

•Accurate predictions: different transient properties ???