[ANSYS, Inc. Logo] return to home search
next up previous contents index

4.7.2 Transport Equations for the Transition SST Model

The transport equation for the intermittency $\gamma$ is defined as:


 \frac{\partial(\rho \gamma)}{\partial t} + \frac{\partial (\... ..._{\gamma}}\right) \frac{\partial \gamma}{\partial x_j}\right] (4.7-1)

The transition sources are defined as follows:


$\displaystyle P_{\gamma 1}$ $\textstyle =$ $\displaystyle 2F_{length}\rho S[\gamma F_{onset}]^{c_{\gamma 3}}$  
$\displaystyle E_{\gamma 1}$ $\textstyle =$ $\displaystyle P_{\gamma 1} \gamma$ (4.7-2)

where $S$ is the strain rate magnitude. $F_{length}$ is an empirical correlation that controls the length of the transition region. The destruction/relaminarization sources are defined as follows:


$\displaystyle P_{\gamma 2}$ $\textstyle =$ $\displaystyle (2c_{\gamma 1})\rho \Omega \gamma F_{turb}$  
$\displaystyle E_{\gamma 2}$ $\textstyle =$ $\displaystyle c_{\gamma 2} P_{\gamma 2} \gamma$ (4.7-3)

where $\Omega$ is the vorticity magnitude. The transition onset is controlled by the following functions:


$\displaystyle Re_V$ $\textstyle =$ $\displaystyle \frac{\rho y^2 S}{\mu}$  
$\displaystyle R_T$ $\textstyle =$ $\displaystyle \frac{\rho k}{\mu \omega}$ (4.7-4)


$\displaystyle F_{onset 1}$ $\textstyle =$ $\displaystyle \frac{Re_v}{2.193 Re_{\theta c}}$  
$\displaystyle F_{onset 2}$ $\textstyle =$ $\displaystyle min(max(F_{onset 1}, F_{onset 1}^4),2.0)$ (4.7-5)


$\displaystyle F_{onset 3}$ $\textstyle =$ $\displaystyle max\left(1-\left(\frac{R_T}{2.5}\right) ^3, 0\right)$  
$\displaystyle F_{onset}$ $\textstyle =$ $\displaystyle max(F_{onset 2} - F_{onset 3}, 0)$  
$\displaystyle F_{turb}$ $\textstyle =$ $\displaystyle e^{-\left(\frac{R_T}{4}\right)^4}$ (4.7-6)

$Re_{\theta c}$ is the critical Reynolds number where the intermittency first starts to increase in the boundary layer. This occurs upstream of the transition Reynolds number $\widetilde{Re_{\theta t}}$ and the difference between the two must be obtained from an empirical correlation. Both the $F_{length}$ and $Re_{\theta c}$ correlations are functions of $\widetilde{Re_{\theta t}}$.

The constants for the intermittency equation are:


c_{\gamma 1} = 0.03; \;\; c_{\gamma 2} = 50; \;\; c_{\gamma 3} = 0.5; \;\; \sigma_{\gamma} = 1.0



Separation Induced Transition Correction


The modification for separation-induced transition is:


$\displaystyle \gamma_{sep}$ $\textstyle =$ $\displaystyle min\left(2 max\left[ \left(\frac{Re_v}{3.235 Re_{\theta c}}\right) -1,0\right] F_{reattch},2\right) F_{\theta t}$  
$\displaystyle F_{reattch}$ $\textstyle =$ $\displaystyle e^{-\left(\frac{R_T}{20}\right)^4}$  
$\displaystyle \gamma_{eff}$ $\textstyle =$ $\displaystyle max(\gamma,\gamma_{sep})$ (4.7-7)

The model constants in Equation  4.7-7 have been adjusted from those of Menter et al. [ 226] in order to improve the predictions of separated flow transition. The main difference is that the constant that controls the relation between $Re_v$ and $Re_{\theta c}$ was changed from 2.193, its value for a Blasius boundary layer, to 3.235, the value at a separation point where the shape factor is 3.5 [ 226]. The boundary condition for $\gamma$ at a wall is zero normal flux, while for an inlet, $\gamma$ is equal to 1.0.

The transport equation for the transition momentum thickness Reynolds number $\widetilde{Re_{\theta t}}$ is


 \frac{\partial (\rho \widetilde{Re_{\theta t}})}{\partial t}... ...frac{\partial \widetilde{Re_{\theta t}}}{\partial x_j}\right] (4.7-8)

The source term is defined as follows:


$\displaystyle P_{\theta t}$ $\textstyle =$ $\displaystyle c_{\theta t} \frac{\rho}{t}(Re_{\theta t} - \widetilde{Re_{\theta t}})(1.0 - F_{\theta t})$  
$\displaystyle t$ $\textstyle =$ $\displaystyle \frac{500 \mu}{\rho U^2}$ (4.7-9)


 F_{\theta t} = min\left(max\left(F_{wake} e^{\left(- \fra... ... \frac{\gamma - 1/50}{1.0-1/50}\right) ^2\right) , 1.0\right) (4.7-10)


$\displaystyle \theta_{BL}$ $\textstyle =$ $\displaystyle \frac{\widetilde{Re_{\theta t}}\mu}{\rho U}$  
$\displaystyle \delta_{BL}$ $\textstyle =$ $\displaystyle \frac{15}{2}\theta_{BL}$ (4.7-11)
$\displaystyle \delta$ $\textstyle =$ $\displaystyle \frac{50 \Omega y}{U}\delta_{BL}$  


$\displaystyle Re_{\omega}$ $\textstyle =$ $\displaystyle \frac{\rho \omega y^2}{\mu}$  
$\displaystyle F_{wake}$ $\textstyle =$ $\displaystyle e^{-\left(\frac{Re_{\omega}}{1E+5}\right)^2}$ (4.7-12)

The model constants for the $\widetilde{Re_{\theta t}}$ equation are:

c_{\theta t} = 0.03 \;\;\; \sigma_{\theta t} = 2.0

The boundary condition for $\widetilde{Re_{\theta t}}$ at a wall is zero flux. The boundary condition for $\widetilde{Re_{\theta t}}$ at an inlet should be calculated from the empirical correlation based on the inlet turbulence intensity.

The model contains three empirical correlations. $Re_{\Theta t}$ is the transition onset as observed in experiments. This has been modified from Menter et al. [ 226] in order to improve the predictions for natural transition. It is used in Equation  4.7-9. $F_{length}$ is the length of the transition zone and is substituted in Equation  4.7-2. $Re_{\Theta c}$ is the point where the model is activated in order to match both $Re_{\Theta t}$ and $F_{length}$, and is used in Equation  4.7-5. At present, these empirical correlations are proprietary and are not given in this manual.


$\displaystyle Re_{\Theta t}$ $\textstyle =$ $\displaystyle f(Tu,\lambda)$  
$\displaystyle F_{length}$ $\textstyle =$ $\displaystyle f(\widetilde{Re_{\Theta t}})$  
$\displaystyle Re_{\Theta c}$ $\textstyle =$ $\displaystyle f(\widetilde{Re_{\Theta t}})$ (4.7-13)

The first empirical correlation is a function of the local turbulence intensity, $Tu$, and the Thwaites' pressure gradient coefficient $\lambda_{\theta}$ is defined as


 \lambda_{\theta} = (\theta^2/v)dU/ds (4.7-14)

where $dU/ds$ is the acceleration in the streamwise direction.



Coupling the Transition Model and SST Transport Equations


The transition model interacts with the SST turbulence model, as follows:


 \frac{\partial}{\partial t}(\rho k) + \frac{\partial}{\parti... ... (\mu + \sigma_k \mu_t)\frac{\partial k}{\partial x_j}\right) (4.7-15)


 \widetilde{P_k} = \gamma_{eff} P_k (4.7-16)


 \widetilde{D_k} = min(max(\gamma_{eff}, 0.1), 1.0)D_k (4.7-17)


 R_y = \frac{\rho y \sqrt{k}}{\mu} (4.7-18)


 F_3 = e^-\left(\frac{R_y}{120}\right)^3 (4.7-19)


 F_t = max(F_{1 orig}, F_3) (4.7-20)

where $P_k$ and $D_k$ are the original production and destruction terms for the SST model and $F_{1orig}$ is the original SST blending function. Note that the production term in the $\omega$-equation is not modified. The rationale behind the above model formulation is given in detail in Menter et al. [ 226].

In order to capture the laminar and transitional boundary layers correctly, the mesh must have a $y^+$ of approximately one. If the $y^+$ is too large (i.e. $>$ 5), then the transition onset location moves upstream with increasing $y^+$. It is recommended to use the bounded second order upwind based discretization for the mean flow, turbulence and transition equations.


next up previous contents index Previous: 4.7.1 Overview
Up: 4.7 Transition SST Model
Next: 4.7.3 Specifying Inlet Turbulence
Release 12.0 © ANSYS, Inc. 2009-01-23