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Simulation and validation of turbulent
gas flow in a cyclone using Caelus
Dr Darrin W Stephens
Dr Chris Sideroff
Prof. Aleksandar Jemcov
Introduction
• Cyclones play a dominant role in industrial
separation of dilute particles from gas flow.
• High swirl and very large curvature of streamlines
presents a modelling challenge.
• Paper’s main objective:
• investigate the effect turbulence model selection has on
the predicted mean flow behaviour within a gas cyclone.
• Numerical simulation results were compared
against experimental data of Witt et al. (1999).
©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015
2
Turbulence models
• Three classes of turbulence models investigated
• Two equation – offer a good compromise between
numerical effort and computational accuracy.
• Reynolds stress - applicable for the flows where the
eddy-viscosity assumption is no longer.
• LES - expected to be more accurate, particularly in
complex flows where the assumptions inherent to RANS
models rarely exist.
©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015
3
Turbulence models cont’d
• Two equation models (k-ω SST):
• Standard: ;
• Spalart and Shur Curvature Correction:
• Hellsten curvature correction
©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015
4
( )( ) ( )* *
min ,10t j j j k t j r kk u k k f P k kν σ ν β ω β ω∂ + ∂ =∂ + ∂ + −
( )( ) ( )
( ) 2
*
2
4 1
min ,10
2 1 .
t j j j t j r k
j j
u f P k
k
F F kφ
ω ω
ω
ω
ω
ω ω ν σ ν ω α β ω
σ
β ω ω
ω
∂ + ∂ =∂ + ∂ +
− + − ∂ ∂
( ){ }max min ,1.25 ,0.0r scale rotationf C f=
( ) ( )
*
1
1 3 2 1*
2
1 1 tan
1
rotation r r r r
r
f c c c r c
r
−
 =+ − − +

4
1
1 RC i
F
C R
=
+
1rf = 4 1F =
1
mag mag
i
mag mag
R
 
= −  
 
Ω Ω
S S
Turbulence models cont’d
• Reynolds stress model:
• Launder Reece Rodi (LRR) pressure strain correlation:
• Omega equation:
©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015
5
*
*2
3
t
t ij k k ij ik k j jk k i ij k k ij
ij
D
R u R R u R u R
k
ν
ν
β
β ωδ
  
∂ + ∂ = − ∂ − ∂ + Π + ∂ + ∂  
  
−
( )
*
1 3 5
4
2
3
ij ij ij ik jk jk ik
ik jk jk ik kl kl ij
C a C kS C k a a
C k a S a S a S
ε
δ
Π =− + + Ω + Ω
 
+ + − 
 
( )( ) 2
2
t j j j t j kku R
k
ω ω ω
ω
ω ω ν σ ν ω α β ω∂ + ∂ =∂ + ∂ + −
2
3
ij
ij ij
R
a
k
δ= −
Turbulence Models cont’d
• LES sub-grid scale (SGS) models
• Unknown stress determined from
• Smagorinsky (1963) – an algebraic model for the SGS
viscosity
• Model parameter Cs is a constant
• Coherent structure (Kobayashi, 2005) – extends
Smagorinsky model using a variable Cs.
;
©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015
6
2 2
SGS s magCν = ∆ S
2ij SGS ijSτ ν= −
( )
3
2 2
1s CSM CS CSC C F F= −
( )
2
i j j i
CS
i j
u u
F
u
−∂ ∂
=
∂
1
22CSMC =
Case Study
• Gas cyclone geometry
• Outer diameter 0.39 m
• Half-angle of 20°
• Bottom outflow is closed for all
simulations.
• Tangential rectangular inlet.
• Grid - 606,264 hexahedral cells
• Uniform inlet velocity of 21.5 m/s.
• Neumann condition applied to all
flow quantities at the vortex finder
outlet.
©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015
7
Numerical Method
• Transient Solver
• SLIM algorithm
• Caelus v5.04 library.
• Discretization
• Time - 2nd order backward scheme
• Gradients - Green-Gauss method.
• Advection - 2nd order linear upwind multidimensional
linear scheme with Barth-Jespersen limiter.
• Courant number - 5 all but RSM (0.5).
• Time averaged for 1000 residence times.
©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015
8
Results
©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015
9
A
B
C
D
E
F
Tangential Vertical
Results cont’d
©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015
10
A
B
C
D
E
F
Tangential Vertical
Results cont’d
©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015
11
A
B
C
D
E
F
Tangential Vertical
Results cont’d
• Non-dimensionalised pressure loss coefficient
• Computational cost
• 60 Intel Xeon E5-2620v3 cores per simulation
©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015
12
Model CPU time (hour) per 1s flow time
SST 1.01
SST-CC 1.14
SST-HELL 1.05
SMAG 1.18
CS 1.48
RSM-LRR 10.90
EXP SST SST-CC SST-HELL SMAG CS RSM-LRR
6.80 10.2 6.02 8.77 6.19 6.56 6.09ξ21
2
in out
in
p p
u
ξ
′ ′−
=
Conclusion
• Turbulent flow inside cyclone simulated with
different turbulence models.
• Turbulence models tested:
• k-ω SST, k-ω SST-CC, k-ω SST-HELL,
• Smagorinsky and Coherent structure LES,
• LRR Reynolds Stress.
• Simulations were performed with a transient
solver using version 5.04 of the Caelus library.
©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015
13
Conclusion
• Comparison with experimental results of Witt et al.
(1999).
• Not suitable for cyclone modelling:
• Standard k-ω SST model
• Hellsten curvature correction
• Most accurate - Coherent structure LES.
• Least accurate - Standard k-ω SST model.
• Most expensive - LRR Reynolds Stress model.
©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015
14
Thank you
Applied CCM
Dr Darrin Stephens
Principal Research Engineer
Phone: 03 8376 6962
Email: d.stephens@appliedccm.com.au
Web: www.appliedccm.com.au
©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015
Questions
15
What is Caelus?
• Caelus was forked from OpenFOAM
• Free and open: www.caelus-cml.com
• Support multiple platforms (Windows, Linux, Mac)
• Easy installation/compilation
• Documentation and validation cases
• Improved algorithmic robustness on non-”perfect” meshes
• Multidimensional interpolation
• Deferred corrections
• Improved accuracy on non-”perfect” meshes
• New compressible solvers
• New turbulence models – VLES, Coherent structure, etc
• Python wrapping, tools and utilities
©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015
16
About Applied CCM
• Specialise in the application, support and development of
OpenFOAM.
• People
• Darrin Stephens, Aleks Jemcov and Chris Sideroff
• Locations
• Australia, USA and Canada
• Engage with customers as their Technology partner
©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015
17

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Simulation and validation of turbulent gas flow in a cyclone using Caelus

  • 1. Simulation and validation of turbulent gas flow in a cyclone using Caelus Dr Darrin W Stephens Dr Chris Sideroff Prof. Aleksandar Jemcov
  • 2. Introduction • Cyclones play a dominant role in industrial separation of dilute particles from gas flow. • High swirl and very large curvature of streamlines presents a modelling challenge. • Paper’s main objective: • investigate the effect turbulence model selection has on the predicted mean flow behaviour within a gas cyclone. • Numerical simulation results were compared against experimental data of Witt et al. (1999). ©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015 2
  • 3. Turbulence models • Three classes of turbulence models investigated • Two equation – offer a good compromise between numerical effort and computational accuracy. • Reynolds stress - applicable for the flows where the eddy-viscosity assumption is no longer. • LES - expected to be more accurate, particularly in complex flows where the assumptions inherent to RANS models rarely exist. ©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015 3
  • 4. Turbulence models cont’d • Two equation models (k-ω SST): • Standard: ; • Spalart and Shur Curvature Correction: • Hellsten curvature correction ©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015 4 ( )( ) ( )* * min ,10t j j j k t j r kk u k k f P k kν σ ν β ω β ω∂ + ∂ =∂ + ∂ + − ( )( ) ( ) ( ) 2 * 2 4 1 min ,10 2 1 . t j j j t j r k j j u f P k k F F kφ ω ω ω ω ω ω ω ν σ ν ω α β ω σ β ω ω ω ∂ + ∂ =∂ + ∂ + − + − ∂ ∂ ( ){ }max min ,1.25 ,0.0r scale rotationf C f= ( ) ( ) * 1 1 3 2 1* 2 1 1 tan 1 rotation r r r r r f c c c r c r −  =+ − − +  4 1 1 RC i F C R = + 1rf = 4 1F = 1 mag mag i mag mag R   = −     Ω Ω S S
  • 5. Turbulence models cont’d • Reynolds stress model: • Launder Reece Rodi (LRR) pressure strain correlation: • Omega equation: ©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015 5 * *2 3 t t ij k k ij ik k j jk k i ij k k ij ij D R u R R u R u R k ν ν β β ωδ    ∂ + ∂ = − ∂ − ∂ + Π + ∂ + ∂      − ( ) * 1 3 5 4 2 3 ij ij ij ik jk jk ik ik jk jk ik kl kl ij C a C kS C k a a C k a S a S a S ε δ Π =− + + Ω + Ω   + + −    ( )( ) 2 2 t j j j t j kku R k ω ω ω ω ω ω ν σ ν ω α β ω∂ + ∂ =∂ + ∂ + − 2 3 ij ij ij R a k δ= −
  • 6. Turbulence Models cont’d • LES sub-grid scale (SGS) models • Unknown stress determined from • Smagorinsky (1963) – an algebraic model for the SGS viscosity • Model parameter Cs is a constant • Coherent structure (Kobayashi, 2005) – extends Smagorinsky model using a variable Cs. ; ©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015 6 2 2 SGS s magCν = ∆ S 2ij SGS ijSτ ν= − ( ) 3 2 2 1s CSM CS CSC C F F= − ( ) 2 i j j i CS i j u u F u −∂ ∂ = ∂ 1 22CSMC =
  • 7. Case Study • Gas cyclone geometry • Outer diameter 0.39 m • Half-angle of 20° • Bottom outflow is closed for all simulations. • Tangential rectangular inlet. • Grid - 606,264 hexahedral cells • Uniform inlet velocity of 21.5 m/s. • Neumann condition applied to all flow quantities at the vortex finder outlet. ©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015 7
  • 8. Numerical Method • Transient Solver • SLIM algorithm • Caelus v5.04 library. • Discretization • Time - 2nd order backward scheme • Gradients - Green-Gauss method. • Advection - 2nd order linear upwind multidimensional linear scheme with Barth-Jespersen limiter. • Courant number - 5 all but RSM (0.5). • Time averaged for 1000 residence times. ©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015 8
  • 9. Results ©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015 9 A B C D E F Tangential Vertical
  • 10. Results cont’d ©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015 10 A B C D E F Tangential Vertical
  • 11. Results cont’d ©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015 11 A B C D E F Tangential Vertical
  • 12. Results cont’d • Non-dimensionalised pressure loss coefficient • Computational cost • 60 Intel Xeon E5-2620v3 cores per simulation ©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015 12 Model CPU time (hour) per 1s flow time SST 1.01 SST-CC 1.14 SST-HELL 1.05 SMAG 1.18 CS 1.48 RSM-LRR 10.90 EXP SST SST-CC SST-HELL SMAG CS RSM-LRR 6.80 10.2 6.02 8.77 6.19 6.56 6.09ξ21 2 in out in p p u ξ ′ ′− =
  • 13. Conclusion • Turbulent flow inside cyclone simulated with different turbulence models. • Turbulence models tested: • k-ω SST, k-ω SST-CC, k-ω SST-HELL, • Smagorinsky and Coherent structure LES, • LRR Reynolds Stress. • Simulations were performed with a transient solver using version 5.04 of the Caelus library. ©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015 13
  • 14. Conclusion • Comparison with experimental results of Witt et al. (1999). • Not suitable for cyclone modelling: • Standard k-ω SST model • Hellsten curvature correction • Most accurate - Coherent structure LES. • Least accurate - Standard k-ω SST model. • Most expensive - LRR Reynolds Stress model. ©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015 14
  • 15. Thank you Applied CCM Dr Darrin Stephens Principal Research Engineer Phone: 03 8376 6962 Email: d.stephens@appliedccm.com.au Web: www.appliedccm.com.au ©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015 Questions 15
  • 16. What is Caelus? • Caelus was forked from OpenFOAM • Free and open: www.caelus-cml.com • Support multiple platforms (Windows, Linux, Mac) • Easy installation/compilation • Documentation and validation cases • Improved algorithmic robustness on non-”perfect” meshes • Multidimensional interpolation • Deferred corrections • Improved accuracy on non-”perfect” meshes • New compressible solvers • New turbulence models – VLES, Coherent structure, etc • Python wrapping, tools and utilities ©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015 16
  • 17. About Applied CCM • Specialise in the application, support and development of OpenFOAM. • People • Darrin Stephens, Aleks Jemcov and Chris Sideroff • Locations • Australia, USA and Canada • Engage with customers as their Technology partner ©Applied CCM. Eleventh International Conference on Computational Fluid Dynamics in the Minerals and Process Industries 2015 17