15aed82e4SJeremy L Thompson // Copyright (c) 2017-2024, Lawrence Livermore National Security, LLC and other CEED contributors. 288626eedSJames Wright // All Rights Reserved. See the top-level LICENSE and NOTICE files for details. 388626eedSJames Wright // 488626eedSJames Wright // SPDX-License-Identifier: BSD-2-Clause 588626eedSJames Wright // 688626eedSJames Wright // This file is part of CEED: http://github.com/ceed 788626eedSJames Wright 888626eedSJames Wright /// @file 988626eedSJames Wright /// Operator for Navier-Stokes example using PETSc 1088626eedSJames Wright #include <ceed.h> 112b730f8bSJeremy L Thompson 122518f336SLeila Ghaffari #include "newtonian_state.h" 13841e4c73SJed Brown #include "newtonian_types.h" 1413fa47b2SJames Wright #include "utils.h" 1588626eedSJames Wright 1607d14e58SLeila Ghaffari #define BLASIUS_MAX_N_CHEBYSHEV 50 1707d14e58SLeila Ghaffari 1888626eedSJames Wright typedef struct BlasiusContext_ *BlasiusContext; 1988626eedSJames Wright struct BlasiusContext_ { 2088626eedSJames Wright bool implicit; // !< Using implicit timesteping or not 21871db79fSKenneth E. Jansen bool weakT; // !< flag to set Temperature weakly at inflow 2288626eedSJames Wright CeedScalar delta0; // !< Boundary layer height at inflow 23fb455ff0SLeila Ghaffari CeedScalar U_inf; // !< Velocity at boundary layer edge 24fb455ff0SLeila Ghaffari CeedScalar T_inf; // !< Temperature at boundary layer edge 252518f336SLeila Ghaffari CeedScalar T_wall; // !< Temperature at the wall 2688626eedSJames Wright CeedScalar P0; // !< Pressure at outflow 27f1122ed0SJames Wright CeedScalar x_inflow; // !< Location of inflow in x 282518f336SLeila Ghaffari CeedScalar n_cheb; // !< Number of Chebyshev terms 2907d14e58SLeila Ghaffari CeedScalar *X; // !< Chebyshev polynomial coordinate vector (CPU only) 302518f336SLeila Ghaffari CeedScalar eta_max; // !< Maximum eta in the domain 3107d14e58SLeila Ghaffari CeedScalar Tf_cheb[BLASIUS_MAX_N_CHEBYSHEV]; // !< Chebyshev coefficient for f 3207d14e58SLeila Ghaffari CeedScalar Th_cheb[BLASIUS_MAX_N_CHEBYSHEV - 1]; // !< Chebyshev coefficient for h 3388626eedSJames Wright struct NewtonianIdealGasContext_ newtonian_ctx; 3488626eedSJames Wright }; 3588626eedSJames Wright 362518f336SLeila Ghaffari // ***************************************************************************** 37ea61e9acSJeremy L Thompson // This helper function evaluates Chebyshev polynomials with a set of coefficients with all their derivatives represented as a recurrence table. 382518f336SLeila Ghaffari // ***************************************************************************** 392b730f8bSJeremy L Thompson CEED_QFUNCTION_HELPER void ChebyshevEval(int N, const double *Tf, double x, double eta_max, double *f) { 402518f336SLeila Ghaffari double dX_deta = 2 / eta_max; 412518f336SLeila Ghaffari double table[4][3] = { 422518f336SLeila Ghaffari // Chebyshev polynomials T_0, T_1, T_2 of the first kind in (-1,1) 432b730f8bSJeremy L Thompson {1, x, 2 * x * x - 1}, 442b730f8bSJeremy L Thompson {0, 1, 4 * x }, 452b730f8bSJeremy L Thompson {0, 0, 4 }, 462b730f8bSJeremy L Thompson {0, 0, 0 } 472518f336SLeila Ghaffari }; 482518f336SLeila Ghaffari for (int i = 0; i < 4; i++) { 492518f336SLeila Ghaffari // i-th derivative of f 502518f336SLeila Ghaffari f[i] = table[i][0] * Tf[0] + table[i][1] * Tf[1] + table[i][2] * Tf[2]; 512518f336SLeila Ghaffari } 522518f336SLeila Ghaffari for (int i = 3; i < N; i++) { 532518f336SLeila Ghaffari // T_n(x) = 2xT_{n-1}(x) - T_{n-2}(x) 542518f336SLeila Ghaffari table[0][i % 3] = 2 * x * table[0][(i - 1) % 3] - table[0][(i - 2) % 3]; 552518f336SLeila Ghaffari // Differentiate Chebyshev polynomials with the recurrence relation 562518f336SLeila Ghaffari for (int j = 1; j < 4; j++) { 572518f336SLeila Ghaffari // T'_{n}(x)/n = 2T_{n-1}(x) + T'_{n-2}(x)/n-2 582518f336SLeila Ghaffari table[j][i % 3] = i * (2 * table[j - 1][(i - 1) % 3] + table[j][(i - 2) % 3] / (i - 2)); 592518f336SLeila Ghaffari } 602518f336SLeila Ghaffari for (int j = 0; j < 4; j++) { 612518f336SLeila Ghaffari f[j] += table[j][i % 3] * Tf[i]; 6288626eedSJames Wright } 6388626eedSJames Wright } 642518f336SLeila Ghaffari for (int i = 1; i < 4; i++) { 652518f336SLeila Ghaffari // Transform derivatives from Chebyshev [-1, 1] to [0, eta_max]. 662518f336SLeila Ghaffari for (int j = 0; j < i; j++) f[i] *= dX_deta; 672518f336SLeila Ghaffari } 6888626eedSJames Wright } 6988626eedSJames Wright 702518f336SLeila Ghaffari // ***************************************************************************** 712518f336SLeila Ghaffari // This helper function computes the Blasius boundary layer solution. 722518f336SLeila Ghaffari // ***************************************************************************** 732b730f8bSJeremy L Thompson State CEED_QFUNCTION_HELPER(BlasiusSolution)(const BlasiusContext blasius, const CeedScalar x[3], const CeedScalar x0, const CeedScalar x_inflow, 7407d14e58SLeila Ghaffari const CeedScalar rho_infty, CeedScalar *t12) { 752518f336SLeila Ghaffari CeedInt N = blasius->n_cheb; 7607d14e58SLeila Ghaffari CeedScalar mu = blasius->newtonian_ctx.mu; 7707d14e58SLeila Ghaffari CeedScalar nu = mu / rho_infty; 78fb455ff0SLeila Ghaffari CeedScalar eta = x[1] * sqrt(blasius->U_inf / (nu * (x0 + x[0] - x_inflow))); 792518f336SLeila Ghaffari CeedScalar X = 2 * (eta / blasius->eta_max) - 1.; 80fb455ff0SLeila Ghaffari CeedScalar U_inf = blasius->U_inf; 812518f336SLeila Ghaffari CeedScalar Rd = GasConstant(&blasius->newtonian_ctx); 822518f336SLeila Ghaffari 832518f336SLeila Ghaffari CeedScalar f[4], h[4]; 842518f336SLeila Ghaffari ChebyshevEval(N, blasius->Tf_cheb, X, blasius->eta_max, f); 852518f336SLeila Ghaffari ChebyshevEval(N - 1, blasius->Th_cheb, X, blasius->eta_max, h); 862518f336SLeila Ghaffari 8707d14e58SLeila Ghaffari *t12 = mu * U_inf * f[2] * sqrt(U_inf / (nu * (x0 + x[0] - x_inflow))); 882518f336SLeila Ghaffari 892518f336SLeila Ghaffari CeedScalar Y[5]; 90fb455ff0SLeila Ghaffari Y[1] = U_inf * f[1]; 91fb455ff0SLeila Ghaffari Y[2] = 0.5 * sqrt(nu * U_inf / (x0 + x[0] - x_inflow)) * (eta * f[1] - f[0]); 922518f336SLeila Ghaffari Y[3] = 0.; 93fb455ff0SLeila Ghaffari Y[4] = blasius->T_inf * h[0]; 9407d14e58SLeila Ghaffari Y[0] = rho_infty / h[0] * Rd * Y[4]; 953bd61617SKenneth E. Jansen return StateFromY(&blasius->newtonian_ctx, Y); 9688626eedSJames Wright } 9788626eedSJames Wright 9888626eedSJames Wright // ***************************************************************************** 9988626eedSJames Wright // This QFunction sets a Blasius boundary layer for the initial condition 10088626eedSJames Wright // ***************************************************************************** 1012b730f8bSJeremy L Thompson CEED_QFUNCTION(ICsBlasius)(void *ctx, CeedInt Q, const CeedScalar *const *in, CeedScalar *const *out) { 10288626eedSJames Wright const CeedScalar(*X)[CEED_Q_VLA] = (const CeedScalar(*)[CEED_Q_VLA])in[0]; 10388626eedSJames Wright CeedScalar(*q0)[CEED_Q_VLA] = (CeedScalar(*)[CEED_Q_VLA])out[0]; 10488626eedSJames Wright 10588626eedSJames Wright const BlasiusContext context = (BlasiusContext)ctx; 106912a746fSJames Wright const NewtonianIdealGasContext gas = &context->newtonian_ctx; 10788626eedSJames Wright const CeedScalar mu = context->newtonian_ctx.mu; 10888626eedSJames Wright const CeedScalar delta0 = context->delta0; 109f1122ed0SJames Wright const CeedScalar x_inflow = context->x_inflow; 1102518f336SLeila Ghaffari CeedScalar t12; 11188626eedSJames Wright 112912a746fSJames Wright const CeedScalar Y_inf[5] = {context->P0, context->U_inf, 0, 0, context->T_inf}; 1133bd61617SKenneth E. Jansen const State s_inf = StateFromY(gas, Y_inf); 11488626eedSJames Wright 115912a746fSJames Wright const CeedScalar x0 = context->U_inf * s_inf.U.density / (mu * 25 / Square(delta0)); 116912a746fSJames Wright 117912a746fSJames Wright CeedPragmaSIMD for (CeedInt i = 0; i < Q; i++) { 118912a746fSJames Wright const CeedScalar x[3] = {X[0][i], X[1][i], X[2][i]}; 119912a746fSJames Wright State s = BlasiusSolution(context, x, x0, x_inflow, s_inf.U.density, &t12); 120912a746fSJames Wright CeedScalar q[5] = {0}; 121912a746fSJames Wright 122912a746fSJames Wright switch (gas->state_var) { 123912a746fSJames Wright case STATEVAR_CONSERVATIVE: 124912a746fSJames Wright UnpackState_U(s.U, q); 125912a746fSJames Wright break; 126912a746fSJames Wright case STATEVAR_PRIMITIVE: 127912a746fSJames Wright UnpackState_Y(s.Y, q); 128912a746fSJames Wright break; 129912a746fSJames Wright } 130912a746fSJames Wright for (CeedInt j = 0; j < 5; j++) q0[j][i] = q[j]; 131912a746fSJames Wright } 13288626eedSJames Wright return 0; 13388626eedSJames Wright } 13488626eedSJames Wright 13588626eedSJames Wright // ***************************************************************************** 1362b730f8bSJeremy L Thompson CEED_QFUNCTION(Blasius_Inflow)(void *ctx, CeedInt Q, const CeedScalar *const *in, CeedScalar *const *out) { 137f21e6b1cSJames Wright const BlasiusContext context = (BlasiusContext)ctx; 13846603fc5SJames Wright const CeedScalar(*q)[CEED_Q_VLA] = (const CeedScalar(*)[CEED_Q_VLA])in[0]; 139f3e15844SJames Wright const CeedScalar(*q_data_sur) = in[2]; 14046603fc5SJames Wright const CeedScalar(*X)[CEED_Q_VLA] = (const CeedScalar(*)[CEED_Q_VLA])in[3]; 14188626eedSJames Wright CeedScalar(*v)[CEED_Q_VLA] = (CeedScalar(*)[CEED_Q_VLA])out[0]; 142f21e6b1cSJames Wright CeedScalar(*jac_data_sur) = context->newtonian_ctx.is_implicit ? out[1] : NULL; 14346603fc5SJames Wright 144f3e15844SJames Wright const bool is_implicit = context->implicit; 145*4c0e8230SJames Wright const NewtonianIdealGasContext gas = &context->newtonian_ctx; 146*4c0e8230SJames Wright const CeedScalar rho_0 = context->P0 / (GasConstant(gas) * context->T_inf); 147*4c0e8230SJames Wright const CeedScalar x0 = context->U_inf * rho_0 / (gas->mu * 25 / Square(context->delta0)); 14829ea4e10SJames Wright const CeedScalar zeros[11] = {0.}; 14988626eedSJames Wright 15046603fc5SJames Wright CeedPragmaSIMD for (CeedInt i = 0; i < Q; i++) { 151f3e15844SJames Wright CeedScalar wdetJb, norm[3]; 152f3e15844SJames Wright QdataBoundaryUnpack_3D(Q, i, q_data_sur, &wdetJb, NULL, norm); 153f3e15844SJames Wright wdetJb *= is_implicit ? -1. : 1.; 15488626eedSJames Wright 155871db79fSKenneth E. Jansen // Calculate inflow values 1562518f336SLeila Ghaffari const CeedScalar x[3] = {X[0][i], X[1][i], 0.}; 15788626eedSJames Wright CeedScalar t12; 158*4c0e8230SJames Wright State s = BlasiusSolution(context, x, x0, context->x_inflow, rho_0, &t12); 15907d14e58SLeila Ghaffari CeedScalar qi[5]; 16007d14e58SLeila Ghaffari for (CeedInt j = 0; j < 5; j++) qi[j] = q[j][i]; 1613bd61617SKenneth E. Jansen State s_int = StateFromU(gas, qi); 16288626eedSJames Wright 163871db79fSKenneth E. Jansen // enabling user to choose between weak T and weak rho inflow 164*4c0e8230SJames Wright if (context->weakT) { // density from the current solution 16507d14e58SLeila Ghaffari s.U.density = s_int.U.density; 1663bd61617SKenneth E. Jansen s.Y = StatePrimitiveFromConservative(gas, s.U); 16707d14e58SLeila Ghaffari } else { // Total energy from current solution 16807d14e58SLeila Ghaffari s.U.E_total = s_int.U.E_total; 1693bd61617SKenneth E. Jansen s.Y = StatePrimitiveFromConservative(gas, s.U); 170871db79fSKenneth E. Jansen } 17107d14e58SLeila Ghaffari 17207d14e58SLeila Ghaffari StateConservative Flux_inviscid[3]; 17307d14e58SLeila Ghaffari FluxInviscid(&context->newtonian_ctx, s, Flux_inviscid); 17488626eedSJames Wright 1752b730f8bSJeremy L Thompson const CeedScalar stress[3][3] = { 1762b730f8bSJeremy L Thompson {0, t12, 0}, 1772b730f8bSJeremy L Thompson {t12, 0, 0}, 1782b730f8bSJeremy L Thompson {0, 0, 0} 1792b730f8bSJeremy L Thompson }; 18007d14e58SLeila Ghaffari const CeedScalar Fe[3] = {0}; // TODO: viscous energy flux needs grad temperature 18107d14e58SLeila Ghaffari CeedScalar Flux[5]; 18207d14e58SLeila Ghaffari FluxTotal_Boundary(Flux_inviscid, stress, Fe, norm, Flux); 1832b730f8bSJeremy L Thompson for (CeedInt j = 0; j < 5; j++) v[j][i] = -wdetJb * Flux[j]; 184f21e6b1cSJames Wright if (is_implicit) StoredValuesPack(Q, i, 0, 11, zeros, jac_data_sur); 185f3e15844SJames Wright } 18688626eedSJames Wright return 0; 18788626eedSJames Wright } 18888626eedSJames Wright 1892518f336SLeila Ghaffari // ***************************************************************************** 1902b730f8bSJeremy L Thompson CEED_QFUNCTION(Blasius_Inflow_Jacobian)(void *ctx, CeedInt Q, const CeedScalar *const *in, CeedScalar *const *out) { 19146603fc5SJames Wright const CeedScalar(*dq)[CEED_Q_VLA] = (const CeedScalar(*)[CEED_Q_VLA])in[0]; 192f3e15844SJames Wright const CeedScalar(*q_data_sur) = in[2]; 19346603fc5SJames Wright const CeedScalar(*X)[CEED_Q_VLA] = (const CeedScalar(*)[CEED_Q_VLA])in[3]; 194e334ad8fSJed Brown CeedScalar(*v)[CEED_Q_VLA] = (CeedScalar(*)[CEED_Q_VLA])out[0]; 19546603fc5SJames Wright 196e334ad8fSJed Brown const BlasiusContext context = (BlasiusContext)ctx; 197*4c0e8230SJames Wright const NewtonianIdealGasContext gas = &context->newtonian_ctx; 198f3e15844SJames Wright const bool is_implicit = context->implicit; 199*4c0e8230SJames Wright const CeedScalar Rd = GasConstant(gas); 200*4c0e8230SJames Wright const CeedScalar gamma = HeatCapacityRatio(gas); 201*4c0e8230SJames Wright const CeedScalar rho_0 = context->P0 / (Rd * context->T_inf); 202*4c0e8230SJames Wright const CeedScalar x0 = context->U_inf * rho_0 / (gas->mu * 25 / (Square(context->delta0))); 203e334ad8fSJed Brown 20446603fc5SJames Wright CeedPragmaSIMD for (CeedInt i = 0; i < Q; i++) { 205f3e15844SJames Wright CeedScalar wdetJb, norm[3]; 206f3e15844SJames Wright QdataBoundaryUnpack_3D(Q, i, q_data_sur, &wdetJb, NULL, norm); 207f3e15844SJames Wright wdetJb *= is_implicit ? -1. : 1.; 208e334ad8fSJed Brown 209e334ad8fSJed Brown // Calculate inflow values 21007d14e58SLeila Ghaffari const CeedScalar x[3] = {X[0][i], X[1][i], X[2][i]}; 211e334ad8fSJed Brown CeedScalar t12; 2122518f336SLeila Ghaffari State s = BlasiusSolution(context, x, x0, 0, rho_0, &t12); 213e334ad8fSJed Brown 214e334ad8fSJed Brown // enabling user to choose between weak T and weak rho inflow 215e334ad8fSJed Brown CeedScalar drho, dE, dP; 216*4c0e8230SJames Wright if (context->weakT) { 217e334ad8fSJed Brown // rho should be from the current solution 218e334ad8fSJed Brown drho = dq[0][i]; 219*4c0e8230SJames Wright CeedScalar dE_internal = drho * gas->cv * context->T_inf; 2202518f336SLeila Ghaffari CeedScalar dE_kinetic = .5 * drho * Dot3(s.Y.velocity, s.Y.velocity); 221e334ad8fSJed Brown dE = dE_internal + dE_kinetic; 222*4c0e8230SJames Wright dP = drho * Rd * context->T_inf; // interior rho with exterior T 223e334ad8fSJed Brown } else { // rho specified, E_internal from solution 224e334ad8fSJed Brown drho = 0; 225e334ad8fSJed Brown dE = dq[4][i]; 226e334ad8fSJed Brown dP = dE * (gamma - 1.); 227e334ad8fSJed Brown } 228e334ad8fSJed Brown 2292518f336SLeila Ghaffari const CeedScalar u_normal = Dot3(norm, s.Y.velocity); 230e334ad8fSJed Brown 231e334ad8fSJed Brown v[0][i] = -wdetJb * drho * u_normal; 2322b730f8bSJeremy L Thompson for (int j = 0; j < 3; j++) { 2332518f336SLeila Ghaffari v[j + 1][i] = -wdetJb * (drho * u_normal * s.Y.velocity[j] + norm[j] * dP); 2342b730f8bSJeremy L Thompson } 235e334ad8fSJed Brown v[4][i] = -wdetJb * u_normal * (dE + dP); 236f3e15844SJames Wright } 237e334ad8fSJed Brown return 0; 238e334ad8fSJed Brown } 239