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Menter's Shear Stress Transport

Menter's Shear Stress Transport turbulence model, or SST, is a widely used and robust two-equation eddy-viscosity turbulence model used in Computational Fluid Dynamics. The model combines the k-omega turbulence model and K-epsilon turbulence model such that the k-omega is used in the inner region of the boundary layer and switches to the k-epsilon in the free shear flow.

History

The SST two equation turbulence model was introduced in 1994 by F.R. Menter to deal with the strong freestream sensitivity of the k-omega turbulence model and improve the predictions of adverse pressure gradients. The formulation of the SST model is based on physical experiments and attempts to predict solutions to typical engineering problems. Over the last two decades the model has been altered to more accurately reflect certain flow conditions. The Reynold's Averaged Eddy-viscosity is a pseudo-force and not physically present in the system. The two variables calculated are usually interpreted so k is the turbulence kinetic energy and omega is the rate of dissipation of the eddies.

SST (Menter’s Shear Stress Transport) turbulence model [1]

 

 

Variable Definition

 

 

 

 

 

 

 

 

 


The constants β, σk, σω are computed by a blend from the corresponding constants via the following formula


 

Constants

K-W Closure

  ,   ,  

K-e Closure

  ,   ,  

SST Closure Constants

  ,  

Boundary and Far Field Conditions

Far Field

 

 

Boundary/Wall Conditions

 

 


Most software implementations like OpenFOAM and ANSYS Fluent do not include the factor of 10 for omega at the wall, following a Wilcox formulation. However in [2] F.R. Menter states: "present author found it much easier and as accurate to implement the following boundary condition"

Validation with experimental results

A good agreement between mass-transfer simulations with experimental data were attained for turbulent flow using the SST two equation turbulence model developed by F.R. Menter for rectangular and tubular shapes,[3] a modified hydrocyclone[4] and for curved rotating systems[5] taking into account a curvature correction term.

References

  1. ^ Menter, F. R. (August 1994). "Two-Equation Eddy-Viscosity Turbulence Models for Engineering Applications". AIAA Journal. 32 (8): 1598–1605. Bibcode:1994AIAAJ..32.1598M. doi:10.2514/3.12149. S2CID 120712103.
  2. ^ Menter, F. R. (July 1993). "Zonal Two Equation k/omega, Turbulence Models for Aerodynamic Flows". AIAA Journal: 1993–2906. doi:10.2514/6.1993-2906. S2CID 130535195.
  3. ^ Colli, A. N.; Bisang, J. M. (January 2018). "A CFD Study with Analytical and Experimental Validation of Laminar and Turbulent Mass-Transfer in Electrochemical Reactors". Journal of the Electrochemical Society. 165 (2): E81–E88. doi:10.1149/2.0971802jes.
  4. ^ Colli, A. N.; Bisang, J. M. (January 2020). "Coupling k Convection-Diffusion and Laplace Equations in an Open-Source CFD Model for Tertiary Current Distribution Calculations". Journal of the Electrochemical Society. 167: 013513. doi:10.1149/2.0132001JES. hdl:11336/150891. S2CID 208732876.
  5. ^ Colli, A. N.; Bisang, J. M. (July 2019). "Time-dependent mass-transfer behaviour under laminar and turbulent flow conditions in rotating electrodes: A CFD study with analytical and experimental validation". International Journal of Heat and Mass Transfer. 137: 835–846. doi:10.1016/j.ijheatmasstransfer.2019.03.152. S2CID 132955462.

Notes

  • 'CFD Online Wilcox k-omega turbulence model description'. Accessed May 12, 2014. http://www.cfd-online.com/Wiki/Wilcox%27s_k-omega_model
  • 'An Introduction to Computational Fluid Dynamics: The Finite Volume Method (2nd Edition)', H. Versteeg, W. Malalasekera; Pearson Education Limited; 2007; ISBN 0131274988
  • 'Turbulence Modeling for CFD' 2nd Ed., Wilcox C. D. ; DCW Industries ; 1998 ; ISBN 0963605100
  • 'An introduction to turbulence and its measurement', Bradshaw, P. ; Pergamon Press ; 1971 ; ISBN 0080166210

menter, shear, stress, transport, turbulence, model, widely, used, robust, equation, eddy, viscosity, turbulence, model, used, computational, fluid, dynamics, model, combines, omega, turbulence, model, epsilon, turbulence, model, such, that, omega, used, inner. Menter s Shear Stress Transport turbulence model or SST is a widely used and robust two equation eddy viscosity turbulence model used in Computational Fluid Dynamics The model combines the k omega turbulence model and K epsilon turbulence model such that the k omega is used in the inner region of the boundary layer and switches to the k epsilon in the free shear flow Contents 1 History 2 SST Menter s Shear Stress Transport turbulence model 1 3 Variable Definition 4 Constants 4 1 K W Closure 4 2 K e Closure 4 3 SST Closure Constants 5 Boundary and Far Field Conditions 5 1 Far Field 5 2 Boundary Wall Conditions 6 Validation with experimental results 7 References 8 NotesHistory EditThe SST two equation turbulence model was introduced in 1994 by F R Menter to deal with the strong freestream sensitivity of the k omega turbulence model and improve the predictions of adverse pressure gradients The formulation of the SST model is based on physical experiments and attempts to predict solutions to typical engineering problems Over the last two decades the model has been altered to more accurately reflect certain flow conditions The Reynold s Averaged Eddy viscosity is a pseudo force and not physically present in the system The two variables calculated are usually interpreted so k is the turbulence kinetic energy and omega is the rate of dissipation of the eddies SST Menter s Shear Stress Transport turbulence model 1 Edit r k t r u j k x j P b r w k x j m s k m t k x j displaystyle frac partial rho k partial t frac partial rho u j k partial x j P beta rho omega k frac partial partial x j left left mu sigma k mu t right frac partial k partial x j right r w t r u j w x j g n t P b r w 2 x j m s w m t w x j 2 1 F 1 r s w 2 w k x j w x j displaystyle frac partial rho omega partial t frac partial rho u j omega partial x j frac gamma nu t P beta rho omega 2 frac partial partial x j left left mu sigma omega mu t right frac partial omega partial x j right 2 1 F 1 frac rho sigma omega 2 omega frac partial k partial x j frac partial omega partial x j Variable Definition EditP t i j u i x j displaystyle P tau ij frac partial u i partial x j t i j m t 2 S i j 2 3 u k x k d i j 2 3 r k d i j displaystyle tau ij mu t left 2S ij frac 2 3 frac partial u k partial x k delta ij right frac 2 3 rho k delta ij S i j 1 2 u i x j u j x i displaystyle S ij frac 1 2 left frac partial u i partial x j frac partial u j partial x i right m t r a 1 k m a x a 1 w W F 2 displaystyle mu t frac rho a 1 k rm max a 1 omega Omega F 2 F 1 t a n h a r g 1 4 displaystyle F 1 rm tanh left rm arg 1 4 right a r g 1 m i n m a x k b w d 500 n d 2 w 4 r s w 2 k C D k w d 2 displaystyle rm arg 1 rm min left rm max left frac sqrt k beta omega d frac 500 nu d 2 omega right frac 4 rho sigma omega 2 k rm CD k omega d 2 right C D k w m a x 2 r s w 2 1 w k x j w x j 10 20 displaystyle rm CD k omega rm max left 2 rho sigma omega 2 frac 1 omega frac partial k partial x j frac partial omega partial x j 10 20 right F 2 t a n h a r g 2 2 displaystyle F 2 rm tanh left rm arg 2 2 right a r g 2 m a x 2 k b w d 500 n d 2 w displaystyle rm arg 2 rm max left 2 frac sqrt k beta omega d frac 500 nu d 2 omega right The constants b sk sw are computed by a blend from the corresponding constants via the following formulaϕ F 1 ϕ 1 1 F 1 ϕ 2 displaystyle phi F 1 phi 1 1 F 1 phi 2 Constants EditK W Closure Edit s k 1 0 85 displaystyle sigma k1 0 85 s w 1 0 65 displaystyle sigma w1 0 65 b 1 0 075 displaystyle beta 1 0 075 K e Closure Edit s k 2 1 00 displaystyle sigma k2 1 00 s w 2 0 856 displaystyle sigma w2 0 856 b 2 0 0828 displaystyle beta 2 0 0828 SST Closure Constants Edit b 0 09 displaystyle beta 0 09 a 1 0 31 displaystyle a 1 0 31 Boundary and Far Field Conditions EditFar Field Edit U L lt w f a r f i e l d lt 10 U L displaystyle frac U infty L lt w rm farfield lt 10 frac U infty L 10 5 U 2 R e L lt k f a r f i e l d lt 0 1 U 2 R e L displaystyle frac 10 5 U infty 2 Re L lt k rm farfield lt frac 0 1U infty 2 Re L Boundary Wall Conditions Edit w w a l l 10 6 n b 1 D d 1 2 displaystyle omega wall 10 frac 6 nu beta 1 Delta d 1 2 k w a l l 0 displaystyle k wall 0 Most software implementations like OpenFOAM and ANSYS Fluent do not include the factor of 10 for omega at the wall following a Wilcox formulation However in 2 F R Menter states present author found it much easier and as accurate to implement the following boundary condition Validation with experimental results EditA good agreement between mass transfer simulations with experimental data were attained for turbulent flow using the SST two equation turbulence model developed by F R Menter for rectangular and tubular shapes 3 a modified hydrocyclone 4 and for curved rotating systems 5 taking into account a curvature correction term References Edit Menter F R August 1994 Two Equation Eddy Viscosity Turbulence Models for Engineering Applications AIAA Journal 32 8 1598 1605 Bibcode 1994AIAAJ 32 1598M doi 10 2514 3 12149 S2CID 120712103 Menter F R July 1993 Zonal Two Equation k omega Turbulence Models for Aerodynamic Flows AIAA Journal 1993 2906 doi 10 2514 6 1993 2906 S2CID 130535195 Colli A N Bisang J M January 2018 A CFD Study with Analytical and Experimental Validation of Laminar and Turbulent Mass Transfer in Electrochemical Reactors Journal of the Electrochemical Society 165 2 E81 E88 doi 10 1149 2 0971802jes Colli A N Bisang J M January 2020 Coupling k Convection Diffusion and Laplace Equations in an Open Source CFD Model for Tertiary Current Distribution Calculations Journal of the Electrochemical Society 167 013513 doi 10 1149 2 0132001JES hdl 11336 150891 S2CID 208732876 Colli A N Bisang J M July 2019 Time dependent mass transfer behaviour under laminar and turbulent flow conditions in rotating electrodes A CFD study with analytical and experimental validation International Journal of Heat and Mass Transfer 137 835 846 doi 10 1016 j ijheatmasstransfer 2019 03 152 S2CID 132955462 Notes Edit CFD Online Wilcox k omega turbulence model description Accessed May 12 2014 http www cfd online com Wiki Wilcox 27s k omega model An Introduction to Computational Fluid Dynamics The Finite Volume Method 2nd Edition H Versteeg W Malalasekera Pearson Education Limited 2007 ISBN 0131274988 Turbulence Modeling for CFD 2nd Ed Wilcox C D DCW Industries 1998 ISBN 0963605100 An introduction to turbulence and its measurement Bradshaw P Pergamon Press 1971 ISBN 0080166210 Retrieved from https en wikipedia org w index php title Menter 27s Shear Stress Transport amp oldid 1117719754, wikipedia, wiki, book, books, library,

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