1(example-petsc-navier-stokes)= 2 3# Compressible Navier-Stokes mini-app 4 5This example is located in the subdirectory {file}`examples/fluids`. 6It solves the time-dependent Navier-Stokes equations of compressible gas dynamics in a static Eulerian three-dimensional frame using unstructured high-order finite/spectral element spatial discretizations and explicit or implicit high-order time-stepping (available in PETSc). 7Moreover, the Navier-Stokes example has been developed using PETSc, so that the pointwise physics (defined at quadrature points) is separated from the parallelization and meshing concerns. 8 9## Running the mini-app 10 11```{include} README.md 12:start-after: inclusion-fluids-marker 13``` 14## The Navier-Stokes equations 15 16The mathematical formulation (from {cite}`giraldoetal2010`, cf. SE3) is given in what follows. 17The compressible Navier-Stokes equations in conservative form are 18 19$$ 20\begin{aligned} 21\frac{\partial \rho}{\partial t} + \nabla \cdot \bm{U} &= 0 \\ 22\frac{\partial \bm{U}}{\partial t} + \nabla \cdot \left( \frac{\bm{U} \otimes \bm{U}}{\rho} + P \bm{I}_3 -\bm\sigma \right) + \rho g \bm{\hat k} &= 0 \\ 23\frac{\partial E}{\partial t} + \nabla \cdot \left( \frac{(E + P)\bm{U}}{\rho} -\bm{u} \cdot \bm{\sigma} - k \nabla T \right) &= 0 \, , \\ 24\end{aligned} 25$$ (eq-ns) 26 27where $\bm{\sigma} = \mu(\nabla \bm{u} + (\nabla \bm{u})^T + \lambda (\nabla \cdot \bm{u})\bm{I}_3)$ is the Cauchy (symmetric) stress tensor, with $\mu$ the dynamic viscosity coefficient, and $\lambda = - 2/3$ the Stokes hypothesis constant. 28In equations {eq}`eq-ns`, $\rho$ represents the volume mass density, $U$ the momentum density (defined as $\bm{U}=\rho \bm{u}$, where $\bm{u}$ is the vector velocity field), $E$ the total energy density (defined as $E = \rho e$, where $e$ is the total energy), $\bm{I}_3$ represents the $3 \times 3$ identity matrix, $g$ the gravitational acceleration constant, $\bm{\hat{k}}$ the unit vector in the $z$ direction, $k$ the thermal conductivity constant, $T$ represents the temperature, and $P$ the pressure, given by the following equation of state 29 30$$ 31P = \left( {c_p}/{c_v} -1\right) \left( E - {\bm{U}\cdot\bm{U}}/{(2 \rho)} - \rho g z \right) \, , 32$$ (eq-state) 33 34where $c_p$ is the specific heat at constant pressure and $c_v$ is the specific heat at constant volume (that define $\gamma = c_p / c_v$, the specific heat ratio). 35 36The system {eq}`eq-ns` can be rewritten in vector form 37 38$$ 39\frac{\partial \bm{q}}{\partial t} + \nabla \cdot \bm{F}(\bm{q}) -S(\bm{q}) = 0 \, , 40$$ (eq-vector-ns) 41 42for the state variables 5-dimensional vector 43 44$$ 45\bm{q} = \begin{pmatrix} \rho \\ \bm{U} \equiv \rho \bm{ u }\\ E \equiv \rho e \end{pmatrix} \begin{array}{l} \leftarrow\textrm{ volume mass density}\\ \leftarrow\textrm{ momentum density}\\ \leftarrow\textrm{ energy density} \end{array} 46$$ 47 48where the flux and the source terms, respectively, are given by 49 50$$ 51\begin{aligned} 52\bm{F}(\bm{q}) &= 53\underbrace{\begin{pmatrix} 54 \bm{U}\\ 55 {(\bm{U} \otimes \bm{U})}/{\rho} + P \bm{I}_3 \\ 56 {(E + P)\bm{U}}/{\rho} 57\end{pmatrix}}_{\bm F_{\text{adv}}} + 58\underbrace{\begin{pmatrix} 590 \\ 60- \bm{\sigma} \\ 61 - \bm{u} \cdot \bm{\sigma} - k \nabla T 62\end{pmatrix}}_{\bm F_{\text{diff}}},\\ 63S(\bm{q}) &= 64- \begin{pmatrix} 65 0\\ 66 \rho g \bm{\hat{k}}\\ 67 0 68\end{pmatrix}. 69\end{aligned} 70$$ (eq-ns-flux) 71 72Let the discrete solution be 73 74$$ 75\bm{q}_N (\bm{x},t)^{(e)} = \sum_{k=1}^{P}\psi_k (\bm{x})\bm{q}_k^{(e)} 76$$ 77 78with $P=p+1$ the number of nodes in the element $e$. 79We use tensor-product bases $\psi_{kji} = h_i(X_0)h_j(X_1)h_k(X_2)$. 80 81For the time discretization, we use two types of time stepping schemes. 82 83- Explicit time-stepping method 84 85 The following explicit formulation is solved with the adaptive Runge-Kutta-Fehlberg (RKF4-5) method by default (any explicit time-stepping scheme available in PETSc can be chosen at runtime) 86 87 $$ 88 \bm{q}_N^{n+1} = \bm{q}_N^n + \Delta t \sum_{i=1}^{s} b_i k_i \, , 89 $$ 90 91 where 92 93 $$ 94 \begin{aligned} 95 k_1 &= f(t^n, \bm{q}_N^n)\\ 96 k_2 &= f(t^n + c_2 \Delta t, \bm{q}_N^n + \Delta t (a_{21} k_1))\\ 97 k_3 &= f(t^n + c_3 \Delta t, \bm{q}_N^n + \Delta t (a_{31} k_1 + a_{32} k_2))\\ 98 \vdots&\\ 99 k_i &= f\left(t^n + c_i \Delta t, \bm{q}_N^n + \Delta t \sum_{j=1}^s a_{ij} k_j \right)\\ 100 \end{aligned} 101 $$ 102 103 and with 104 105 $$ 106 f(t^n, \bm{q}_N^n) = - [\nabla \cdot \bm{F}(\bm{q}_N)]^n + [S(\bm{q}_N)]^n \, . 107 $$ 108 109- Implicit time-stepping method 110 111 This time stepping method which can be selected using the option `-implicit` is solved with Backward Differentiation Formula (BDF) method by default (similarly, any implicit time-stepping scheme available in PETSc can be chosen at runtime). 112 The implicit formulation solves nonlinear systems for $\bm q_N$: 113 114 $$ 115 \bm f(\bm q_N) \equiv \bm g(t^{n+1}, \bm{q}_N, \bm{\dot{q}}_N) = 0 \, , 116 $$ (eq-ts-implicit-ns) 117 118 where the time derivative $\bm{\dot q}_N$ is defined by 119 120 $$ 121 \bm{\dot{q}}_N(\bm q_N) = \alpha \bm q_N + \bm z_N 122 $$ 123 124 in terms of $\bm z_N$ from prior state and $\alpha > 0$, both of which depend on the specific time integration scheme (backward difference formulas, generalized alpha, implicit Runge-Kutta, etc.). 125 Each nonlinear system {eq}`eq-ts-implicit-ns` will correspond to a weak form, as explained below. 126 In determining how difficult a given problem is to solve, we consider the Jacobian of {eq}`eq-ts-implicit-ns`, 127 128 $$ 129 \frac{\partial \bm f}{\partial \bm q_N} = \frac{\partial \bm g}{\partial \bm q_N} + \alpha \frac{\partial \bm g}{\partial \bm{\dot q}_N}. 130 $$ 131 132 The scalar "shift" $\alpha$ scales inversely with the time step $\Delta t$, so small time steps result in the Jacobian being dominated by the second term, which is a sort of "mass matrix", and typically well-conditioned independent of grid resolution with a simple preconditioner (such as Jacobi). 133 In contrast, the first term dominates for large time steps, with a condition number that grows with the diameter of the domain and polynomial degree of the approximation space. 134 Both terms are significant for time-accurate simulation and the setup costs of strong preconditioners must be balanced with the convergence rate of Krylov methods using weak preconditioners. 135 136To obtain a finite element discretization, we first multiply the strong form {eq}`eq-vector-ns` by a test function $\bm v \in H^1(\Omega)$ and integrate, 137 138$$ 139\int_{\Omega} \bm v \cdot \left(\frac{\partial \bm{q}_N}{\partial t} + \nabla \cdot \bm{F}(\bm{q}_N) - \bm{S}(\bm{q}_N) \right) \,dV = 0 \, , \; \forall \bm v \in \mathcal{V}_p\,, 140$$ 141 142with $\mathcal{V}_p = \{ \bm v(\bm x) \in H^{1}(\Omega_e) \,|\, \bm v(\bm x_e(\bm X)) \in P_p(\bm{I}), e=1,\ldots,N_e \}$ a mapped space of polynomials containing at least polynomials of degree $p$ (with or without the higher mixed terms that appear in tensor product spaces). 143 144Integrating by parts on the divergence term, we arrive at the weak form, 145 146$$ 147\begin{aligned} 148\int_{\Omega} \bm v \cdot \left( \frac{\partial \bm{q}_N}{\partial t} - \bm{S}(\bm{q}_N) \right) \,dV 149- \int_{\Omega} \nabla \bm v \!:\! \bm{F}(\bm{q}_N)\,dV & \\ 150+ \int_{\partial \Omega} \bm v \cdot \bm{F}(\bm q_N) \cdot \widehat{\bm{n}} \,dS 151 &= 0 \, , \; \forall \bm v \in \mathcal{V}_p \,, 152\end{aligned} 153$$ (eq-weak-vector-ns) 154 155where $\bm{F}(\bm q_N) \cdot \widehat{\bm{n}}$ is typically replaced with a boundary condition. 156 157:::{note} 158The notation $\nabla \bm v \!:\! \bm F$ represents contraction over both fields and spatial dimensions while a single dot represents contraction in just one, which should be clear from context, e.g., $\bm v \cdot \bm S$ contracts over fields while $\bm F \cdot \widehat{\bm n}$ contracts over spatial dimensions. 159::: 160 161We solve {eq}`eq-weak-vector-ns` using a Galerkin discretization (default) or a stabilized method, as is necessary for most real-world flows. 162 163Galerkin methods produce oscillations for transport-dominated problems (any time the cell Péclet number is larger than 1), and those tend to blow up for nonlinear problems such as the Euler equations and (low-viscosity/poorly resolved) Navier-Stokes, in which case stabilization is necessary. 164Our formulation follows {cite}`hughesetal2010`, which offers a comprehensive review of stabilization and shock-capturing methods for continuous finite element discretization of compressible flows. 165 166- **SUPG** (streamline-upwind/Petrov-Galerkin) 167 168 In this method, the weighted residual of the strong form {eq}`eq-vector-ns` is added to the Galerkin formulation {eq}`eq-weak-vector-ns`. 169 The weak form for this method is given as 170 171 $$ 172 \begin{aligned} 173 \int_{\Omega} \bm v \cdot \left( \frac{\partial \bm{q}_N}{\partial t} - \bm{S}(\bm{q}_N) \right) \,dV 174 - \int_{\Omega} \nabla \bm v \!:\! \bm{F}(\bm{q}_N)\,dV & \\ 175 + \int_{\partial \Omega} \bm v \cdot \bm{F}(\bm{q}_N) \cdot \widehat{\bm{n}} \,dS & \\ 176 + \int_{\Omega} \nabla\bm v \tcolon\left(\frac{\partial \bm F_{\text{adv}}}{\partial \bm q}\right) \bm\tau \left( \frac{\partial \bm{q}_N}{\partial t} \, + \, 177 \nabla \cdot \bm{F} \, (\bm{q}_N) - \bm{S}(\bm{q}_N) \right) \,dV &= 0 178 \, , \; \forall \bm v \in \mathcal{V}_p 179 \end{aligned} 180 $$ (eq-weak-vector-ns-supg) 181 182 This stabilization technique can be selected using the option `-stab supg`. 183 184- **SU** (streamline-upwind) 185 186 This method is a simplified version of *SUPG* {eq}`eq-weak-vector-ns-supg` which is developed for debugging/comparison purposes. The weak form for this method is 187 188 $$ 189 \begin{aligned} 190 \int_{\Omega} \bm v \cdot \left( \frac{\partial \bm{q}_N}{\partial t} - \bm{S}(\bm{q}_N) \right) \,dV 191 - \int_{\Omega} \nabla \bm v \!:\! \bm{F}(\bm{q}_N)\,dV & \\ 192 + \int_{\partial \Omega} \bm v \cdot \bm{F}(\bm{q}_N) \cdot \widehat{\bm{n}} \,dS & \\ 193 + \int_{\Omega} \nabla\bm v \tcolon\left(\frac{\partial \bm F_{\text{adv}}}{\partial \bm q}\right) \bm\tau \nabla \cdot \bm{F} \, (\bm{q}_N) \,dV 194 & = 0 \, , \; \forall \bm v \in \mathcal{V}_p 195 \end{aligned} 196 $$ (eq-weak-vector-ns-su) 197 198 This stabilization technique can be selected using the option `-stab su`. 199 200In both {eq}`eq-weak-vector-ns-su` and {eq}`eq-weak-vector-ns-supg`, $\bm\tau \in \mathbb R^{5\times 5}$ (field indices) is an intrinsic time scale matrix. 201The SUPG technique and the operator $\frac{\partial \bm F_{\text{adv}}}{\partial \bm q}$ (rather than its transpose) can be explained via an ansatz for subgrid state fluctuations $\tilde{\bm q} = -\bm\tau \bm r$ where $\bm r$ is a strong form residual. 202The forward variational form can be readily expressed by differentiating $\bm F_{\text{adv}}$ of {eq}`eq-ns-flux` 203 204$$ 205\begin{aligned} 206\diff\bm F_{\text{adv}}(\diff\bm q; \bm q) &= \frac{\partial \bm F_{\text{adv}}}{\partial \bm q} \diff\bm q \\ 207&= \begin{pmatrix} 208\diff\bm U \\ 209(\diff\bm U \otimes \bm U + \bm U \otimes \diff\bm U)/\rho - (\bm U \otimes \bm U)/\rho^2 \diff\rho + \diff P \bm I_3 \\ 210(E + P)\diff\bm U/\rho + (\diff E + \diff P)\bm U/\rho - (E + P) \bm U/\rho^2 \diff\rho 211\end{pmatrix}, 212\end{aligned} 213$$ 214 215where $\diff P$ is defined by differentiating {eq}`eq-state`. 216 217:::{dropdown} Stabilization scale $\bm\tau$ 218A velocity vector $\bm u$ can be pulled back to the reference element as $\bm u_{\bm X} = \nabla_{\bm x}\bm X \cdot \bm u$, with units of reference length (non-dimensional) per second. 219To build intuition, consider a boundary layer element of dimension $(1, \epsilon)$, for which $\nabla_{\bm x} \bm X = \bigl(\begin{smallmatrix} 2 & \\ & 2/\epsilon \end{smallmatrix}\bigr)$. 220So a small normal component of velocity will be amplified (by a factor of the aspect ratio $1/\epsilon$) in this transformation. 221The ratio $\lVert \bm u \rVert / \lVert \bm u_{\bm X} \rVert$ is a covariant measure of (half) the element length in the direction of the velocity. 222A contravariant measure of element length in the direction of a unit vector $\hat{\bm n}$ is given by $\lVert \bigl(\nabla_{\bm X} \bm x\bigr)^T \hat{\bm n} \rVert$. 223While $\nabla_{\bm X} \bm x$ is readily computable, its inverse $\nabla_{\bm x} \bm X$ is needed directly in finite element methods and thus more convenient for our use. 224If we consider a parallelogram, the covariant measure is larger than the contravariant measure for vectors pointing between acute corners and the opposite holds for vectors between oblique corners. 225 226The cell Péclet number is classically defined by $\mathrm{Pe}_h = \lVert \bm u \rVert h / (2 \kappa)$ where $\kappa$ is the diffusivity (units of $m^2/s$). 227This can be generalized to arbitrary grids by defining the local Péclet number 228 229$$ 230\mathrm{Pe} = \frac{\lVert \bm u \rVert^2}{\lVert \bm u_{\bm X} \rVert \kappa}. 231$$ (eq-peclet) 232 233For scalar advection-diffusion, the stabilization is a scalar 234 235$$ 236\tau = \frac{\xi(\mathrm{Pe})}{\lVert \bm u_{\bm X} \rVert}, 237$$ (eq-tau-advdiff) 238 239where $\xi(\mathrm{Pe}) = \coth \mathrm{Pe} - 1/\mathrm{Pe}$ approaches 1 at large local Péclet number. 240Note that $\tau$ has units of time and, in the transport-dominated limit, is proportional to element transit time in the direction of the propagating wave. 241For advection-diffusion, $\bm F(q) = \bm u q$, and thus the SU stabilization term is 242 243$$ 244\nabla v \cdot \bm u \tau \bm u \cdot \nabla q = \nabla_{\bm X} v \cdot (\bm u_{\bm X} \tau \bm u_{\bm X}) \cdot \nabla_{\bm X} q . 245$$ (eq-su-stabilize-advdiff) 246 247where the term in parentheses is a rank-1 diffusivity tensor that has been pulled back to the reference element. 248See {cite}`hughesetal2010` equations 15-17 and 34-36 for further discussion of this formulation. 249 250For the Navier-Stokes and Euler equations, {cite}`whiting2003hierarchical` defines a $5\times 5$ diagonal stabilization $\mathrm{diag}(\tau_c, \tau_m, \tau_m, \tau_m, \tau_E)$ consisting of 2511. continuity stabilization $\tau_c$ 2522. momentum stabilization $\tau_m$ 2533. energy stabilization $\tau_E$ 254 255The Navier-Stokes code in this example uses the following formulation for $\tau_c$, $\tau_m$, $\tau_E$: 256 257$$ 258\begin{aligned} 259 260\tau_c &= \frac{C_c \mathcal{F}}{8\rho \trace(\bm g)} \\ 261\tau_m &= \frac{C_m}{\mathcal{F}} \\ 262\tau_E &= \frac{C_E}{\mathcal{F} c_v} \\ 263\end{aligned} 264$$ 265 266$$ 267\mathcal{F} = \sqrt{ \rho^2 \left [ \left(\frac{2C_t}{\Delta t}\right)^2 268+ \bm u \cdot (\bm u \cdot \bm g) 269+ C_v \mu^2 \Vert \bm g \Vert_F ^2\right]} 270$$ 271 272where $\bm g = \nabla_{\bm x} \bm{X} \cdot \nabla_{\bm x} \bm{X}$ is the metric tensor and $\Vert \cdot \Vert_F$ is the Frobenius norm. 273This formulation is currently not available in the Euler code. 274 275In the Euler code, we follow {cite}`hughesetal2010` in defining a $3\times 3$ diagonal stabilization according to spatial criterion 2 (equation 27) as follows. 276 277$$ 278\tau_{ii} = c_{\tau} \frac{2 \xi(\mathrm{Pe})}{(\lambda_{\max \text{abs}})_i \lVert \nabla_{x_i} \bm X \rVert} 279$$ (eq-tau-conservative) 280 281where $c_{\tau}$ is a multiplicative constant reported to be optimal at 0.5 for linear elements, $\hat{\bm n}_i$ is a unit vector in direction $i$, and $\nabla_{x_i} = \hat{\bm n}_i \cdot \nabla_{\bm x}$ is the derivative in direction $i$. 282The flux Jacobian $\frac{\partial \bm F_{\text{adv}}}{\partial \bm q} \cdot \hat{\bm n}_i$ in each direction $i$ is a $5\times 5$ matrix with spectral radius $(\lambda_{\max \text{abs}})_i$ equal to the fastest wave speed. 283The complete set of eigenvalues of the Euler flux Jacobian in direction $i$ are (e.g., {cite}`toro2009`) 284 285$$ 286\Lambda_i = [u_i - a, u_i, u_i, u_i, u_i+a], 287$$ (eq-eigval-advdiff) 288 289where $u_i = \bm u \cdot \hat{\bm n}_i$ is the velocity component in direction $i$ and $a = \sqrt{\gamma P/\rho}$ is the sound speed for ideal gasses. 290Note that the first and last eigenvalues represent nonlinear acoustic waves while the middle three are linearly degenerate, carrying a contact wave (temperature) and transverse components of momentum. 291The fastest wave speed in direction $i$ is thus 292 293$$ 294\lambda_{\max \text{abs}} \Bigl( \frac{\partial \bm F_{\text{adv}}}{\partial \bm q} \cdot \hat{\bm n}_i \Bigr) = |u_i| + a 295$$ (eq-wavespeed) 296 297Note that this wave speed is specific to ideal gases as $\gamma$ is an ideal gas parameter; other equations of state will yield a different acoustic wave speed. 298 299::: 300 301Currently, this demo provides three types of problems/physical models that can be selected at run time via the option `-problem`. 302{ref}`problem-advection`, the problem of the transport of energy in a uniform vector velocity field, {ref}`problem-euler-vortex`, the exact solution to the Euler equations, and the so called {ref}`problem-density-current` problem. 303 304(problem-advection)= 305 306## Advection 307 308A simplified version of system {eq}`eq-ns`, only accounting for the transport of total energy, is given by 309 310$$ 311\frac{\partial E}{\partial t} + \nabla \cdot (\bm{u} E ) = 0 \, , 312$$ (eq-advection) 313 314with $\bm{u}$ the vector velocity field. In this particular test case, a blob of total energy (defined by a characteristic radius $r_c$) is transported by two different wind types. 315 316- **Rotation** 317 318 In this case, a uniform circular velocity field transports the blob of total energy. 319 We have solved {eq}`eq-advection` applying zero energy density $E$, and no-flux for $\bm{u}$ on the boundaries. 320 321- **Translation** 322 323 In this case, a background wind with a constant rectilinear velocity field, enters the domain and transports the blob of total energy out of the domain. 324 325 For the inflow boundary conditions, a prescribed $E_{wind}$ is applied weakly on the inflow boundaries such that the weak form boundary integral in {eq}`eq-weak-vector-ns` is defined as 326 327 $$ 328 \int_{\partial \Omega_{inflow}} \bm v \cdot \bm{F}(\bm q_N) \cdot \widehat{\bm{n}} \,dS = \int_{\partial \Omega_{inflow}} \bm v \, E_{wind} \, \bm u \cdot \widehat{\bm{n}} \,dS \, , 329 $$ 330 331 For the outflow boundary conditions, we have used the current values of $E$, following {cite}`papanastasiou1992outflow` which extends the validity of the weak form of the governing equations to the outflow instead of replacing them with unknown essential or natural boundary conditions. 332 The weak form boundary integral in {eq}`eq-weak-vector-ns` for outflow boundary conditions is defined as 333 334 $$ 335 \int_{\partial \Omega_{outflow}} \bm v \cdot \bm{F}(\bm q_N) \cdot \widehat{\bm{n}} \,dS = \int_{\partial \Omega_{outflow}} \bm v \, E \, \bm u \cdot \widehat{\bm{n}} \,dS \, , 336 $$ 337 338(problem-euler-vortex)= 339 340## Isentropic Vortex 341 342Three-dimensional Euler equations, which are simplified and nondimensionalized version of system {eq}`eq-ns` and account only for the convective fluxes, are given by 343 344$$ 345\begin{aligned} 346\frac{\partial \rho}{\partial t} + \nabla \cdot \bm{U} &= 0 \\ 347\frac{\partial \bm{U}}{\partial t} + \nabla \cdot \left( \frac{\bm{U} \otimes \bm{U}}{\rho} + P \bm{I}_3 \right) &= 0 \\ 348\frac{\partial E}{\partial t} + \nabla \cdot \left( \frac{(E + P)\bm{U}}{\rho} \right) &= 0 \, , \\ 349\end{aligned} 350$$ (eq-euler) 351 352Following the setup given in {cite}`zhang2011verification`, the mean flow for this problem is $\rho=1$, $P=1$, $T=P/\rho= 1$ (Specific Gas Constant, $R$, is 1), and $\bm{u}=(u_1,u_2,0)$ while the perturbation $\delta \bm{u}$, and $\delta T$ are defined as 353 354$$ 355\begin{aligned} (\delta u_1, \, \delta u_2) &= \frac{\epsilon}{2 \pi} \, e^{0.5(1-r^2)} \, (-\bar{y}, \, \bar{x}) \, , \\ \delta T &= - \frac{(\gamma-1) \, \epsilon^2}{8 \, \gamma \, \pi^2} \, e^{1-r^2} \, , \\ \end{aligned} 356$$ 357 358where $(\bar{x}, \, \bar{y}) = (x-x_c, \, y-y_c)$, $(x_c, \, y_c)$ represents the center of the domain, $r^2=\bar{x}^2 + \bar{y}^2$, and $\epsilon$ is the vortex strength ($\epsilon$ < 10). 359There is no perturbation in the entropy $S=P/\rho^\gamma$ ($\delta S=0)$. 360 361(problem-shock-tube)= 362 363## Shock Tube 364 365This test problem is based on Sod's Shock Tube (from{cite}`sodshocktubewiki`), a canonical test case for discontinuity capturing in one dimension. For this problem, the three-dimensional Euler equations are formulated exactly as in the Isentropic Vortex problem. The default initial conditions are $P=1$, $\rho=1$ for the driver section and $P=0.1$, $\rho=0.125$ for the driven section. The initial velocity is zero in both sections. Slip boundary conditions are applied to the side walls and wall boundary conditions are applied at the end walls. 366 367SU upwinding and discontinuity capturing have been implemented into the explicit timestepping operator for this problem. Discontinuity capturing is accomplished using a modified version of the $YZ\beta$ operator described in {cite}`tezduyar2007yzb`. This discontinuity capturing scheme involves the introduction of a dissipation term of the form 368 369$$ 370\int_{\Omega} \nu_{SHOCK} \nabla \bm v \!:\! \nabla \bm q dV 371$$ 372 373The shock capturing viscosity is implemented following the first formulation described in {cite}`tezduyar2007yzb`. The characteristic velocity $u_{cha}$ is taken to be the acoustic speed while the reference density $\rho_{ref}$ is just the local density. Shock capturing viscosity is defined by the following 374 375$$ 376\nu_{SHOCK} = \tau_{SHOCK} u_{cha}^2 377$$ 378 379where, 380 381$$ 382\tau_{SHOCK} = \frac{h_{SHOCK}}{2u_{cha}} \left( \frac{ \,|\, \nabla \rho \,|\, h_{SHOCK}}{\rho_{ref}} \right)^{\beta} 383$$ 384 385$\beta$ is a tuning parameter set between 1 (smoother shocks) and 2 (sharper shocks. The parameter $h_{SHOCK}$ is a length scale that is proportional to the element length in the direction of the density gradient unit vector. This density gradient unit vector is defined as $\hat{\bm j} = \frac{\nabla \rho}{|\nabla \rho|}$. The original formulation of Tezduyar and Senga relies on the shape function gradient to define the element length scale, but this gradient is not available to qFunctions in libCEED. To avoid this problem, $h_{SHOCK}$ is defined in the current implementation as 386 387$$ 388h_{SHOCK} = 2 \left( C_{YZB} \,|\, \bm p \,|\, \right)^{-1} 389$$ 390 391where 392 393$$ 394p_k = \hat{j}_i \frac{\partial \xi_i}{x_k} 395$$ 396 397The constant $C_{YZB}$ is set to 0.1 for piecewise linear elements in the current implementation. Larger values approaching unity are expected with more robust stabilization and implicit timestepping. 398 399(problem-density-current)= 400 401## Newtonian Wave 402This test case is taken/inspired by that presented in {cite}`mengaldoCompressibleBC2014`. It is intended to test non-reflecting/Riemann boundary conditions. It's primarily intended for Euler equations, but has been implemented for the Navier-Stokes equations here for flexibility. 403 404The problem has a perturbed initial condition and lets it evolve in time. The initial condition contains a Gaussian perturbation in the pressure field: 405 406$$ 407\begin{aligned} 408\rho &= \rho_\infty\left(1+A\exp\left(\frac{-(\bar{x}^2 + \bar{y}^2)}{2\sigma^2}\right)\right) \\ 409\bm{U} &= \bm U_\infty \\ 410E &= \frac{p_\infty}{\gamma -1}\left(1+A\exp\left(\frac{-(\bar{x}^2 + \bar{y}^2)}{2\sigma^2}\right)\right) + \frac{\bm U_\infty \cdot \bm U_\infty}{2\rho_\infty}, 411\end{aligned} 412$$ 413 414where $A$ and $\sigma$ are the amplitude and width of the perturbation, respectively, and $(\bar{x}, \bar{y}) = (x-x_e, y-y_e)$ is the distance to the epicenter of the perturbation, $(x_e, y_e)$. 415The simulation produces a strong acoustic wave and leaves behind a cold thermal bubble that advects at the fluid velocity. 416 417The boundary conditions are freestream in the x and y directions. When using an HLL (Harten, Lax, van Leer) Riemann solver {cite}`toro2009` (option `-freestream_riemann hll`), the acoustic waves exit the domain cleanly, but when the thermal bubble reaches the boundary, it produces strong thermal oscillations that become acoustic waves reflecting into the domain. 418This problem can be fixed using a more sophisticated Riemann solver such as HLLC {cite}`toro2009` (option `-freestream_riemann hllc`, which is default), which is a linear constant-pressure wave that transports temperature and transverse momentum at the fluid velocity. 419 420## Vortex Shedding - Flow past Cylinder 421This test case, based on {cite}`shakib1991femcfd`, is an example of using an externally provided mesh from Gmsh. 422A cylinder with diameter $D=1$ is centered at $(0,0)$ in a computational domain $-4.5 \leq x \leq 15.5$, $-4.5 \leq y \leq 4.5$. 423We solve this as a 3D problem with (default) one element in the $z$ direction. 424The domain is filled with an ideal gas at rest (zero velocity) with temperature 24.92 and pressure 7143. 425The viscosity is 0.01 and thermal conductivity is 14.34 to maintain a Prandtl number of 0.71, which is typical for air. 426At time $t=0$, this domain is subjected to freestream boundary conditions at the inflow (left) and Riemann-type outflow on the right, with exterior reference state at velocity $(1, 0, 0)$ giving Reynolds number $100$ and Mach number $0.01$. 427A symmetry (adiabatic free slip) condition is imposed at the top and bottom boundaries $(y = \pm 4.5)$ (zero normal velocity component, zero heat-flux). 428The cylinder wall is an adiabatic (no heat flux) no-slip boundary condition. 429As we evolve in time, eddies appear past the cylinder leading to a vortex shedding known as the vortex street, with shedding period of about 6. 430 431The Gmsh input file, `examples/fluids/meshes/cylinder.geo` is parametrized to facilitate experimenting with similar configurations. 432The Strouhal number (nondimensional shedding frequency) is sensitive to the size of the computational domain and boundary conditions. 433 434Forces on the cylinder walls are computed using the "reaction force" method, which is variationally consistent with the volume operator. 435Given the force components $\bm F = (F_x, F_y, F_z)$ and surface area $S = \pi D L_z$ where $L_z$ is the spanwise extent of the domain, we define the coefficients of lift and drag as 436 437$$ 438\begin{aligned} 439C_L &= \frac{2 F_y}{\rho_\infty u_\infty^2 S} \\ 440C_D &= \frac{2 F_x}{\rho_\infty u_\infty^2 S} \\ 441\end{aligned} 442$$ 443 444where $\rho_\infty, u_\infty$ are the freestream (inflow) density and velocity respectively. 445 446## Density Current 447 448For this test problem (from {cite}`straka1993numerical`), we solve the full Navier-Stokes equations {eq}`eq-ns`, for which a cold air bubble (of radius $r_c$) drops by convection in a neutrally stratified atmosphere. 449Its initial condition is defined in terms of the Exner pressure, $\pi(\bm{x},t)$, and potential temperature, $\theta(\bm{x},t)$, that relate to the state variables via 450 451$$ 452\begin{aligned} \rho &= \frac{P_0}{( c_p - c_v)\theta(\bm{x},t)} \pi(\bm{x},t)^{\frac{c_v}{ c_p - c_v}} \, , \\ e &= c_v \theta(\bm{x},t) \pi(\bm{x},t) + \bm{u}\cdot \bm{u} /2 + g z \, , \end{aligned} 453$$ 454 455where $P_0$ is the atmospheric pressure. 456For this problem, we have used no-slip and non-penetration boundary conditions for $\bm{u}$, and no-flux for mass and energy densities. 457 458## Channel 459 460A compressible channel flow. Analytical solution given in 461{cite}`whitingStabilizedFEM1999`: 462 463$$ u_1 = u_{\max} \left [ 1 - \left ( \frac{x_2}{H}\right)^2 \right] \quad \quad u_2 = u_3 = 0$$ 464$$T = T_w \left [ 1 + \frac{Pr \hat{E}c}{3} \left \{1 - \left(\frac{x_2}{H}\right)^4 \right \} \right]$$ 465$$p = p_0 - \frac{2\rho_0 u_{\max}^2 x_1}{Re_H H}$$ 466 467where $H$ is the channel half-height, $u_{\max}$ is the center velocity, $T_w$ is the temperature at the wall, $Pr=\frac{\mu}{c_p \kappa}$ is the Prandlt number, $\hat E_c = \frac{u_{\max}^2}{c_p T_w}$ is the modified Eckert number, and $Re_h = \frac{u_{\max}H}{\nu}$ is the Reynolds number. 468 469Boundary conditions are periodic in the streamwise direction, and no-slip and non-penetration boundary conditions at the walls. 470The flow is driven by a body force determined analytically from the fluid properties and setup parameters $H$ and $u_{\max}$. 471 472## Flat Plate Boundary Layer 473 474### Laminar Boundary Layer - Blasius 475 476Simulation of a laminar boundary layer flow, with the inflow being prescribed 477by a [Blasius similarity 478solution](https://en.wikipedia.org/wiki/Blasius_boundary_layer). At the inflow, 479the velocity is prescribed by the Blasius soution profile, density is set 480constant, and temperature is allowed to float. Using `weakT: true`, density is 481allowed to float and temperature is set constant. At the outlet, a user-set 482pressure is used for pressure in the inviscid flux terms (all other inviscid 483flux terms use interior solution values). The wall is a no-slip, 484no-penetration, no-heat flux condition. The top of the domain is treated as an 485outflow and is tilted at a downward angle to ensure that flow is always exiting 486it. 487 488### Turbulent Boundary Layer 489 490Simulating a turbulent boundary layer without modeling the turbulence requires 491resolving the turbulent flow structures. These structures may be introduced 492into the simulations either by allowing a laminar boundary layer naturally 493transition to turbulence, or imposing turbulent structures at the inflow. The 494latter approach has been taken here, specifically using a *synthetic turbulence 495generation* (STG) method. 496 497#### Synthetic Turbulence Generation (STG) Boundary Condition 498 499We use the STG method described in 500{cite}`shurSTG2014`. Below follows a re-description of the formulation to match 501the present notation, and then a description of the implementation and usage. 502 503##### Equation Formulation 504 505$$ 506\bm{u}(\bm{x}, t) = \bm{\overline{u}}(\bm{x}) + \bm{C}(\bm{x}) \cdot \bm{v}' 507$$ 508 509$$ 510\begin{aligned} 511\bm{v}' &= 2 \sqrt{3/2} \sum^N_{n=1} \sqrt{q^n(\bm{x})} \bm{\sigma}^n \cos(\kappa^n \bm{d}^n \cdot \bm{\hat{x}}^n(\bm{x}, t) + \phi^n ) \\ 512\bm{\hat{x}}^n &= \left[(x - U_0 t)\max(2\kappa_{\min}/\kappa^n, 0.1) , y, z \right]^T 513\end{aligned} 514$$ 515 516Here, we define the number of wavemodes $N$, set of random numbers $ \{\bm{\sigma}^n, 517\bm{d}^n, \phi^n\}_{n=1}^N$, the Cholesky decomposition of the Reynolds stress 518tensor $\bm{C}$ (such that $\bm{R} = \bm{CC}^T$ ), bulk velocity $U_0$, 519wavemode amplitude $q^n$, wavemode frequency $\kappa^n$, and $\kappa_{\min} = 5200.5 \min_{\bm{x}} (\kappa_e)$. 521 522$$ 523\kappa_e = \frac{2\pi}{\min(2d_w, 3.0 l_t)} 524$$ 525 526where $l_t$ is the turbulence length scale, and $d_w$ is the distance to the 527nearest wall. 528 529 530The set of wavemode frequencies is defined by a geometric distribution: 531 532$$ 533\kappa^n = \kappa_{\min} (1 + \alpha)^{n-1} \ , \quad \forall n=1, 2, ... , N 534$$ 535 536The wavemode amplitudes $q^n$ are defined by a model energy spectrum $E(\kappa)$: 537 538$$ 539q^n = \frac{E(\kappa^n) \Delta \kappa^n}{\sum^N_{n=1} E(\kappa^n)\Delta \kappa^n} \ ,\quad \Delta \kappa^n = \kappa^n - \kappa^{n-1} 540$$ 541 542$$ E(\kappa) = \frac{(\kappa/\kappa_e)^4}{[1 + 2.4(\kappa/\kappa_e)^2]^{17/6}} f_\eta f_{\mathrm{cut}} $$ 543 544$$ 545f_\eta = \exp \left[-(12\kappa /\kappa_\eta)^2 \right], \quad 546f_\mathrm{cut} = \exp \left( - \left [ \frac{4\max(\kappa-0.9\kappa_\mathrm{cut}, 0)}{\kappa_\mathrm{cut}} \right]^3 \right) 547$$ 548 549$\kappa_\eta$ represents turbulent dissipation frequency, and is given as $2\pi 550(\nu^3/\varepsilon)^{-1/4}$ with $\nu$ the kinematic viscosity and 551$\varepsilon$ the turbulent dissipation. $\kappa_\mathrm{cut}$ approximates the 552effective cutoff frequency of the mesh (viewing the mesh as a filter on 553solution over $\Omega$) and is given by: 554 555$$ 556\kappa_\mathrm{cut} = \frac{2\pi}{ 2\min\{ [\max(h_y, h_z, 0.3h_{\max}) + 0.1 d_w], h_{\max} \} } 557$$ 558 559The enforcement of the boundary condition is identical to the blasius inflow; 560it weakly enforces velocity, with the option of weakly enforcing either density 561or temperature using the the `-weakT` flag. 562 563##### Initialization Data Flow 564 565Data flow for initializing function (which creates the context data struct) is 566given below: 567```{mermaid} 568flowchart LR 569 subgraph STGInflow.dat 570 y 571 lt[l_t] 572 eps 573 Rij[R_ij] 574 ubar 575 end 576 577 subgraph STGRand.dat 578 rand[RN Set]; 579 end 580 581 subgraph User Input 582 u0[U0]; 583 end 584 585 subgraph init[Create Context Function] 586 ke[k_e] 587 N; 588 end 589 lt --Calc-->ke --Calc-->kn 590 y --Calc-->ke 591 592 subgraph context[Context Data] 593 yC[y] 594 randC[RN Set] 595 Cij[C_ij] 596 u0 --Copy--> u0C[U0] 597 kn[k^n]; 598 ubarC[ubar] 599 ltC[l_t] 600 epsC[eps] 601 end 602 ubar --Copy--> ubarC; 603 y --Copy--> yC; 604 lt --Copy--> ltC; 605 eps --Copy--> epsC; 606 607 rand --Copy--> randC; 608 rand --> N --Calc--> kn; 609 Rij --Calc--> Cij[C_ij] 610``` 611 612This is done once at runtime. The spatially-varying terms are then evaluated at 613each quadrature point on-the-fly, either by interpolation (for $l_t$, 614$\varepsilon$, $C_{ij}$, and $\overline{\bm u}$) or by calculation (for $q^n$). 615 616The `STGInflow.dat` file is a table of values at given distances from the wall. 617These values are then interpolated to a physical location (node or quadrature 618point). It has the following format: 619``` 620[Total number of locations] 14 621[d_w] [u_1] [u_2] [u_3] [R_11] [R_22] [R_33] [R_12] [R_13] [R_23] [sclr_1] [sclr_2] [l_t] [eps] 622``` 623where each `[ ]` item is a number in scientific notation (ie. `3.1415E0`), and `sclr_1` and 624`sclr_2` are reserved for turbulence modeling variables. They are not used in 625this example. 626 627The `STGRand.dat` file is the table of the random number set, $\{\bm{\sigma}^n, 628\bm{d}^n, \phi^n\}_{n=1}^N$. It has the format: 629``` 630[Number of wavemodes] 7 631[d_1] [d_2] [d_3] [phi] [sigma_1] [sigma_2] [sigma_3] 632``` 633 634The following table is presented to help clarify the dimensionality of the 635numerous terms in the STG formulation. 636 637| Math | Label | $f(\bm{x})$? | $f(n)$? | 638|-----------------|--------|--------------|---------| 639| $ \{\bm{\sigma}^n, \bm{d}^n, \phi^n\}_{n=1}^N$ | RN Set | No | Yes | 640| $\bm{\overline{u}}$ | ubar | Yes | No | 641| $U_0$ | U0 | No | No | 642| $l_t$ | l_t | Yes | No | 643| $\varepsilon$ | eps | Yes | No | 644| $\bm{R}$ | R_ij | Yes | No | 645| $\bm{C}$ | C_ij | Yes | No | 646| $q^n$ | q^n | Yes | Yes | 647| $\{\kappa^n\}_{n=1}^N$ | k^n | No | Yes | 648| $h_i$ | h_i | Yes | No | 649| $d_w$ | d_w | Yes | No | 650 651### Meshing 652 653The flat plate boundary layer example has custom meshing features to better 654resolve the flow. One of those is tilting the top of the domain, allowing for 655it to be a outflow boundary condition. The angle of this tilt is controlled by 656`-platemesh_top_angle` 657 658The primary meshing feature is the ability to grade the mesh, providing better 659resolution near the wall. There are two methods to do this; algorithmically, or 660specifying the node locations via a file. Algorithmically, a base node 661distribution is defined at the inlet (assumed to be $\min(x)$) and then 662linearly stretched/squeezed to match the slanted top boundary condition. Nodes 663are placed such that `-platemesh_Ndelta` elements are within 664`-platemesh_refine_height` of the wall. They are placed such that the element 665height matches a geometric growth ratio defined by `-platemesh_growth`. The 666remaining elements are then distributed from `-platemesh_refine_height` to the 667top of the domain linearly in logarithmic space. 668 669Alternatively, a file may be specified containing the locations of each node. 670The file should be newline delimited, with the first line specifying the number 671of points and the rest being the locations of the nodes. The node locations 672used exactly at the inlet (assumed to be $\min(x)$) and linearly 673stretched/squeezed to match the slanted top boundary condition. The file is 674specified via `-platemesh_y_node_locs_path`. If this flag is given an empty 675string, then the algorithmic approach will be performed. 676