Computational domain and solver setup
A structured grid 2D C-H topology quadrilateral mesh was generated around UBD5494 airfoil in the mesh generating tool ICEM-CFD. Quadrilateral-type cell was chosen because it can provide high-quality solution with less number of cells compared to the triangle mesh [24]. Moreover, in order to attain a fully developed and expanded flow, the length of the computational domain was made 40 times that of the chord length of the airfoil, whereas the width is kept 30 times. To ensure the computed aerodynamic results are independent of the grid size, the density of grid was increased until negligible difference in solution is attained towards convergence. Such methodology of optimum grid selection is adapted from [35, 36].
At the outset, the coarse gird named as Grid 1 containing 50,365 cells was made. Number of cells was increased to 70,827 in Grid 2, whereas Grid 3 and Grid 4 contained 108,562 and 130,204 cells, respectively. For all the grids, the mesh density in the attached boundary layer was increased to capture the transition, flow separation and most importantly the predicted separation bubble. The mesh density was kept progressively coarser in the far-field area where the flow gradients approaches zero. Dense grids, with increased number of cells, were also placed near the leading and trailing edge because of the steepest gradients. The transition in mesh size was kept as smooth as possible for numerical accuracy. The boundary conditions for the inlet were taken as velocity inlet and the outlet conditions were defined as the pressure outlet.
The solver was set for steady state. Desired angle of attack, α, was attained by rotating the mesh in order to capture the movement of possible separation bubble and the stall angle. Velocity at inlet was specified to achieve the desired Re. To solve the coupled problem between pressure in momentum equations and velocity components, semi-implicit method for pressure-linked equations (SIMPLE) algorithm [24] was employed, and second-order upwind spatial discretization was set in calculation. The spatial gradient was selected as the least squares cell based. Air pressure was taken as standard. Convergence criteria residual target values were set to 10−6. For precise simulation of the boundary-layer flows and the coupled lift and drag forces of airfoils, y+, which is a non-dimensional distance from the wall to the first node of the mesh was satisfied with the value of y+ <1 (Fig. 3).
As shown in Fig. 4a and b, difference in the aerodynamic lift and drag coefficients for α = 7° becomes negligible from Grid 2 onwards. Thus, the refined Grid 3, with 108,562 cells, was adopted for numerical experimentation. Image of Grid 3 is shown in Fig. 5. Final Numerical analysis on the airfoil was performed using ANSYS-Fulent at Re = 6 × 104, 1 × 105, 1.5 × 105, 2 × 105 and 3 × 105 with the above-mentioned solver settings.
Turbulence model
Transport equations
In the present work, transition model \(\gamma - {\text{Re}}_{\theta }\) is used to incorporate turbulence in the flow. It is a four equation turbulence model that combines Shear Stress Transport k-omega turbulence model (SST k-ω) transport equations with two additional transport equations, one for intermittency (\(\gamma\)) and second for Transition Reynolds number (Re
θt). Here, intermittency term is employed to activate the production term of the turbulent kinetic energy (TKE), downstream of the transition point in the boundary layer, whereas the Transition Reynolds number term captures the non-local effect of the turbulence intensity [21]. This model is reported to have a distinct advantage of associating transition modelling with experimental data [21–24]. Moreover, according to [21–24], the transport equation for intermittency, \(\gamma ,\) read as
$$\frac{{\partial \left( {\rho \gamma } \right)}}{\partial t} + \frac{{\partial \left( {\rho U_{\text{j}} \gamma } \right)}}{{\partial x_{\text{j}} }} = P_{\gamma 1} - E_{\gamma 1} + P_{\gamma 2} - E_{\gamma 2} + \frac{\partial }{{\partial x_{\text{j}} }}\left[ {\left( {\mu + \frac{{\mu_{\text{t}} }}{{\sigma_{\gamma } }}} \right)\frac{\partial \gamma }{{\partial x_{\text{j}} }}} \right],$$
(4)
\({\text{where}} \; \mu\) is the molecular viscosity (Pa.s) and \(\mu_{\text{t}}\) is the eddy viscosity (Pa.s). The transition sources, \(P_{\gamma 1} \;{\text{and}}\;E_{\gamma 1} ,\) are defined as
$$P_{\gamma 1} = F_{\text{lenght}} c_{{{\text{a}}1}} \rho S\left[ {\gamma F_{\text{onset}} } \right]^{{c_{\text{a}} }}$$
(5)
$$E_{\gamma 1} = c_{\text{e1}} P_{\gamma 1} \gamma.$$
(6)
And the destruction sources, \(P_{\gamma 2} \;{\text{and}}\;E_{\gamma 2} ,\) are defined as
$$P_{{\gamma 2}} = {\it c}_{{\rm a2}} \rho {\it F}_{{\rm turb}}\,{\Omega }$$
(7)
$$E_{\gamma 2} = c_{{{\text{e}}2}} P_{\gamma 2} \gamma,$$
(8)
where S represents the strain rate (s−1) and \(F_{\text{lenght}}\) is the empirical correlation to control the length of the transition region. The term Ω represents the vorticity magnitude. The terms \(c_{\text{e1}} , c_{{{\text{a}}1}} , c_{{{\text{e}}2}} , c_{\alpha } , \sigma_{\varUpsilon }\) are constants in the intermittency equation, with values
$$c_{\text{e1}} = 1.0 ; c_{{{\text{a}}1}} = 2.0 ;c_{\text{e2}} = 50 ; c_{\text{a2}} = 0.06 ,c_{\alpha } = 0.5, \sigma_{\varUpsilon } = 1.0.$$
The \(F_{\text{onset}}\) determines when the production of \(\gamma , {\text{the intermittency}},\) is activated. The functions to control transition onset are given by
$$\text{Re}_{\text{V}} = \frac{{\rho y^{2} S}}{\mu }; \quad {{\text{Re}}}_{\text{T}} = \frac{\rho k}{\mu \omega }$$
(9)
$$F_{{{\text{onset}}1}} = \frac{{{\text{Re}}_{\text{v}} }}{{2.193\text{Re}_{{\theta {\text{c}}}} }}$$
(10)
$$F_{\text{onset2}} = \hbox{min} \left( {\hbox{max} \left( {F_{\text{onset1}} ,F_{\text{onset1}}^{4} } \right),2.0} \right)$$
(11)
$$F_{\text{onset3}} = \hbox{max} \left( {1 - \left( {\frac{{R_{\text{T}} }}{2.5}} \right)^{3} ,0} \right)$$
(12)
$$F_{\text{onset}} = \hbox{max} \left( {F_{\text{onset2}} - F_{\text{onset3}} ,0} \right).$$
(13)
\(\text{Re}_{{\theta {\text{c}}}}\) is the critical Reynolds number where intermittency begins to increase in the boundary layer. This happens upstream of the transition Reynolds number \({\tilde{\text{R}}\text{e}}_{{\theta {\text{t}}}}\) and the difference between the two must be obtained from an empirical correlation [21–23]. Both the \(\text{Re}_{{\theta {\text{c}}}}\) correlations are functions of \({\tilde{\text{R}}\text{e}}_{{\theta {\text{t}}}} .\) The term \(\text{Re}_{\text{T}}\) is the viscosity ratio and \(\text{Re}_{\text{V}}\) is the strain rate (vorticity) Reynolds number, whereas \(k\) is the TKE (J kg−1) and \(\omega\) represents the specific turbulence dissipation rate (m2s−1).
Separation-induced transition modification
The tailored separation-induced transition is written as
$$\gamma_{\text{sep}} = \hbox{min} \left[ {2 \cdot \hbox{max} \left[ {\left( {\frac{{{\text{Re}}_{\text{v}} }}{{3.235 {\text{Re}}_{{\theta {\text{c}}}} }}} \right) - 1,0} \right]F_{\text{reattach}} ,2 } \right]F_{{\theta {\text{t}}}} ;$$
(14)
$$F_{\text{reattach}} = {\text{e}}^{{ - \left( {\frac{{\text{R}_{\text{T}} }}{20}} \right)^{4} }} ;$$
(15)
$$\gamma_{\text{eff}} = \hbox{max} \left( {\gamma , \gamma_{\text{sep}} } \right).$$
(16)
Once the viscosity ratio is large enough to force reattachment, \(F_{\text{reattach}}\) disables the modification. \(F_{{\theta {\text{t}}}}\) is the blending function used to turn off the source term in the boundary layer:
$$F_{{\theta {\text{t}}}} = \hbox{min} \left( {\hbox{max} \left( {F_{\text{wake}} \cdot {\text{e}}^{{ - \left( {\frac{y}{\delta }} \right)^{4} }} ,1.0 - \left( {\frac{{\gamma - \frac{1}{{c_{{{\text{e}}2}} }}}}{{1.0 - \frac{1}{{c_{{{\text{e}}2}} }}}}} \right)^{2} } \right),1.0} \right)$$
(17)
$$\delta = \frac{500\varOmega y }{U}.\delta_{\text{BL}} ; \delta_{\text{BL}} = \frac{15}{2}\theta_{\text{BL}} ; \theta_{\text{BL}} = \frac{{\mu {\tilde{\text{R}}\text{e}}_{{\theta {\text{t}}}} }}{\rho U}$$
(18)
$$F_{\text{wake}} = {\text{e}}^{{ - \left( {\frac{{{\text{Re}}_{\omega } }}{{1{\text{E}} + 5}}} \right)^{2} }} ; {\text{Re}}_{\omega } = \frac{{\rho \omega y^{2} }}{\mu }.$$
(19)
\(F_{\text{wake}}\) ensures that the blending function are not active downstream of an airfoil. The transport equation for transition momentum thickness number, \({\tilde{\text{R}}\text{e}}_{{\theta {\text{t}}}} ,\) is expressed as
$$\frac{{\partial \left( {\rho {\tilde{\text{R}}\text{e}}_{{\theta {\text{t}}}} } \right)}}{\partial t} + \frac{{\partial \left( { \rho U_{\text{j}} {\tilde{\text{R}}\text{e}}_{{\theta {\text{t}}}} } \right)}}{{\partial x_{\text{j}} }} = P_{{\theta {\text{t }}}} + \frac{\partial }{{\partial x_{\text{j}} }}\left[ {\sigma_{{\theta {\text{t}}}} \left( {\mu + \mu_{\text{t}} } \right)\frac{{\partial {\tilde{\text{R}}\text{e}}_{{\theta {\text{t}}}} }}{{\partial x_{\text{j}} }}} \right].$$
(20)
The source term, \(P_{{\theta {\text{t}}}} ,\) is defined as
$$P_{{\theta {\text{t}}}} = c_{{\theta {\text{t}}}} \frac{\rho }{t}\left( {{{\text{Re}}}_{{\theta {\text{t}}}} - {\tilde{\text{R}}\text{e}}_{{\theta {\text{t}}}} } \right)\left( {1.0 - F_{{\theta {\text{t}}}} } \right).$$
(21)
Here,
$$t = \frac{500\mu }{{\rho U^{2} }}.$$
The parameter t is determined using dimensional analysis. The values of the constants \(c_{{\theta {\text{t}}}} \; {\text{and}}\; \sigma_{{\theta {\text{t}}}}\) in the Reynolds momentum thickness are given in [21–24] as
$$c_{{\theta {\text{t}}}} = 0.03 ; \sigma_{{\theta {\text{t}}}} = 2.0,$$
where term \(c_{{\theta {\text{t}}}}\) controls the magnitude of source terms and \(\sigma_{{\theta {\text{t}}}}\) controls the diffusion coefficient. These constants values in the original model were derived on flat plate transition experimentation [23]. However, in order to obtain physically realistic solution, modified constants based on low Re simulations [33] of circular arc airfoils are adapted in the present work, given as
$$c_{{\theta {\text{t}}}} = 0.02;\; \sigma_{{\theta {\text{t}}}} = 3.0.$$
Coupling transition model and SST transport equations
Finally, the transition model interacts with SST transition model as
$$\frac{\partial }{\partial t}\left( {\rho k} \right) + \frac{\partial }{{\partial x_{\text{i}} }}\left( {\rho ku_{\text{i}} } \right) = \frac{\partial }{{\partial x_{\text{i}} }}\left( {\varGamma_{\text{k}} \frac{\partial k}{{\partial x_{\text{j}} }}} \right) + G_{\text{k}}^{*} - Y_{\text{k}}^{*} + S_{\text{k}}$$
(22)
$$Y_{\text{k}}^{*} = \hbox{min} \left( {{ \hbox{max} }\left( {\gamma_{\text{eff}} ,0.1} \right),1.0} \right)Y_{\text{k}}$$
$$G_{\text{k}}^{*} = \gamma_{\text{eff}} G_{\text{k}},$$
where Y
k and G
k are the original terms of SST model for destruction and production, respectively. The production term in the ω equation was unchanged.