# Zeta-f model

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 Revision as of 12:28, 22 January 2007 (view source) (→The elliptic relaxation function $f$)← Older edit Latest revision as of 10:06, 17 December 2008 (view source)Peter (Talk | contribs) m (Reverted edits by TadelBasno (Talk) to last version by Jola) (12 intermediate revisions not shown) Line 1: Line 1: - The ''zeta-f'' model is a robust modification of the elliptic relaxation model. The set of equations, for the incompressible Newtonian fluid, constituting the $\zeta-f$ model is given below. + The ''zeta-f'' model is a robust modification of the elliptic relaxation model. For the incompressible Newtonian fluid the final set of equations constituting the $\zeta-f$ model is given below. Line 22: Line 22: $L^2 \nabla^2 f - f = \frac{1}{T} \left( C_1 - 1 + C'_2 \frac{P_k}{\varepsilon} \right) \left( \zeta - \frac{2}{3} \right)$ $L^2 \nabla^2 f - f = \frac{1}{T} \left( C_1 - 1 + C'_2 \frac{P_k}{\varepsilon} \right) \left( \zeta - \frac{2}{3} \right)$ - == The production of the turbulent kinetic energy $P_k$ == + == Production of the turbulent kinetic energy $P_k$ == :$:[itex] - P_k = - \overline{u_i u_j} \frac{\partial u_j}{\partial x_i} + P_k = - \overline{u_i u_j} \frac{\partial U_j}{\partial x_i}$ [/itex]

:$P_k = \nu_t S^2$ :$P_k = \nu_t S^2$ + == Modulus of the mean rate-of-strain tensor $S$ == - == The modulus of the mean rate-of-strain tensor $S$ == + $S \equiv \sqrt{2S_{ij} S_{ij}}$ -
+ - :$+ - S \equiv \sqrt{2S_{ij} S_{ij}} + -$ + + == Turbulence time scale $T$ == - == The turbulence time scale $T$ == + $T = max \left[ min \left( \frac{k}{\varepsilon},\, \frac{0.6}{\sqrt{6} C_{\mu} |S|\zeta} \right), C_T \left( \frac{\nu}{\varepsilon} \right)^{1/2} \right]$ - $T = max \left[ min \left( \frac{k}{\varepsilon},\, \frac{0.6}{\sqrt{6} C_{\mu} |S|\zeta} \right), C_T \left( \frac{\nu^3}{\varepsilon} \right)^{1/2} \right]$ + == Turbulence length scale $L$ == - + - + - == The turbulence length scale $L$ == + $L = C_L \, max \left[ min \left( \frac{k^{3/2}}{\varepsilon}, \, [itex]L = C_L \, max \left[ min \left( \frac{k^{3/2}}{\varepsilon}, \, Line 49: Line 44: \left( \frac{\nu^3}{\varepsilon} \right)^{1/4} \right]$ \left( \frac{\nu^3}{\varepsilon} \right)^{1/4} \right][/itex] - + == Model coefficients == - == The coefficients == + $C_\mu = 0.22$, $\sigma_{k} = 1$, $\sigma_{\varepsilon} = 1.3$, $\sigma_{\zeta} = 1.2$, $C_{\varepsilon 1} = 1.4 (1 + 0.012 / \zeta)$, $C_{\varepsilon 2} = 1.9$, $C_1 = 1.4$, $C_2' = 0.65$, $C_T = 6$, $C_L = 0.36$ and $C_{\eta} = 85$. $C_\mu = 0.22$, $\sigma_{k} = 1$, $\sigma_{\varepsilon} = 1.3$, $\sigma_{\zeta} = 1.2$, $C_{\varepsilon 1} = 1.4 (1 + 0.012 / \zeta)$, $C_{\varepsilon 2} = 1.9$, $C_1 = 1.4$, $C_2' = 0.65$, $C_T = 6$, $C_L = 0.36$ and $C_{\eta} = 85$. - == References == == References == - *Popovac, M., Hanjalic, K. Compound Wall Treatment for RANS Computation of Complex Turbulent Flows and Heat Transfer, Flow, Turbulence and Combustion, DOI 10.1007/s10494-006-9067-x, 2007. + *Popovac, M., Hanjalic, K. Compound Wall Treatment for RANS Computation of Complex Turbulent Flows and Heat Transfer, Flow Turbulence and Combustion, 78, 177-202, 2007. *Hanjalic, K., Popovac, M., Hadziabdic, M. A robust near-wall elliptic-relaxation eddy-viscosity turbulence model for CFD, Int. J. Heat Fluid Flow, 25, 1047–1051, 2004. *Hanjalic, K., Popovac, M., Hadziabdic, M. A robust near-wall elliptic-relaxation eddy-viscosity turbulence model for CFD, Int. J. Heat Fluid Flow, 25, 1047–1051, 2004. + + [[Category:Turbulence models]] {{stub}} {{stub}} - [[Category:Turbulence models]]

## Latest revision as of 10:06, 17 December 2008

The zeta-f model is a robust modification of the elliptic relaxation model. For the incompressible Newtonian fluid the final set of equations constituting the $\zeta-f$ model is given below.

## Turbulent viscosity $\nu_t$

$\nu_t = C_\mu \, \zeta \, k \, T$

## Turbulent kinetic energy $k$

$\frac{\partial k}{\partial t} + U_j \frac{\partial k}{\partial x_j} = P_k - \varepsilon + \frac{\partial}{\partial x_j} \left[ \left( \nu + \frac{\nu_t}{\sigma_{k}} \right) \frac{\partial k}{\partial x_j} \right]$

## Turbulent kinetic energy dissipation rate $\varepsilon$

$\frac{\partial \varepsilon}{\partial t} + U_j \frac{\partial \varepsilon}{\partial x_j} = \frac{C_{\varepsilon 1} P_k - C_{\varepsilon 2} \varepsilon}{T} + \frac{\partial}{\partial x_j} \left[ \left( \nu + \frac{\nu_t}{\sigma_{\varepsilon}} \right) \frac{\partial \varepsilon}{\partial x_j} \right]$

## Normalized velocity scale $\zeta$

$\frac{\partial \zeta}{\partial t} + U_j \frac{\partial \zeta}{\partial x_j} = f - \frac{\zeta}{k} P_k + \frac{\partial}{\partial x_j} \left[ \left( \nu + \frac{\nu_t}{\sigma_{\zeta}} \right) \frac{\partial \zeta}{\partial x_j} \right]$

## Elliptic relaxation function $f$

$L^2 \nabla^2 f - f = \frac{1}{T} \left( C_1 - 1 + C'_2 \frac{P_k}{\varepsilon} \right) \left( \zeta - \frac{2}{3} \right)$

## Production of the turbulent kinetic energy $P_k$

$P_k = - \overline{u_i u_j} \frac{\partial U_j}{\partial x_i}$

$P_k = \nu_t S^2$

## Modulus of the mean rate-of-strain tensor $S$

$S \equiv \sqrt{2S_{ij} S_{ij}}$

## Turbulence time scale $T$

$T = max \left[ min \left( \frac{k}{\varepsilon},\, \frac{0.6}{\sqrt{6} C_{\mu} |S|\zeta} \right), C_T \left( \frac{\nu}{\varepsilon} \right)^{1/2} \right]$

## Turbulence length scale $L$

$L = C_L \, max \left[ min \left( \frac{k^{3/2}}{\varepsilon}, \, \frac{k^{1/2}}{\sqrt{6} C_{\mu} |S| \zeta} \right), C_{\eta} \left( \frac{\nu^3}{\varepsilon} \right)^{1/4} \right]$

## Model coefficients

$C_\mu = 0.22$, $\sigma_{k} = 1$, $\sigma_{\varepsilon} = 1.3$, $\sigma_{\zeta} = 1.2$, $C_{\varepsilon 1} = 1.4 (1 + 0.012 / \zeta)$, $C_{\varepsilon 2} = 1.9$, $C_1 = 1.4$, $C_2' = 0.65$, $C_T = 6$, $C_L = 0.36$ and $C_{\eta} = 85$.

## References

• Popovac, M., Hanjalic, K. Compound Wall Treatment for RANS Computation of Complex Turbulent Flows and Heat Transfer, Flow Turbulence and Combustion, 78, 177-202, 2007.
• Hanjalic, K., Popovac, M., Hadziabdic, M. A robust near-wall elliptic-relaxation eddy-viscosity turbulence model for CFD, Int. J. Heat Fluid Flow, 25, 1047–1051, 2004.