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Searched refs:temperature (Results 1 – 17 of 17) sorted by relevance

/honee/problems/ !
H A Dbc_outflow.c126 CeedScalar temperature = reference->temperature / units->Kelvin; in OutflowBCSetup() local
133 …-outflow_temperature", "Temperature at outflow condition", NULL, temperature, &temperature, NULL)); in OutflowBCSetup()
141 temperature *= units->Kelvin; in OutflowBCSetup()
149 .temperature = temperature, in OutflowBCSetup()
H A Dblasius.c27 …PetscScalar Ma = Mach(gas, S_infty.Y.temperature, U_infty), Pr = Prandtl(gas), gamma = HeatCapacit… in CompressibleBlasiusResidual()
61 r[N] = h[0] - blasius->T_wall / S_infty.Y.temperature; in CompressibleBlasiusResidual()
188 .temperature = T_inf in NS_BLASIUS()
221 PetscCall(SetupStg(comm, dm, problem, honee, weakT, S_infty.Y.temperature, S_infty.Y.pressure)); in NS_BLASIUS()
H A Dbc_freestream.c125 … = reference->pressure / units->Pascal, .velocity = {0}, .temperature = reference->temperature / u… in FreestreamBCSetup()
134 …erature", "Temperature at freestream condition", NULL, Y_inf.temperature, &Y_inf.temperature, NULL… in FreestreamBCSetup()
139 Y_inf.temperature *= units->Kelvin; in FreestreamBCSetup()
H A Dnewtonian.c385 StatePrimitive reference = {.pressure = 1.01e5, .velocity = {0}, .temperature = 288.15}; in NS_NEWTONIAN_IG()
446 …erature", "Reference/initial temperature", NULL, reference.temperature, &reference.temperature, NU… in NS_NEWTONIAN_IG()
484 reference.temperature *= units->Kelvin; in NS_NEWTONIAN_IG()
/honee/qfunctions/ !
H A Dnewtonian_state.h33 Y[4] = s.temperature; in UnpackState_Y()
54 CeedScalar e_internal = gas.cv * s.Y.temperature; in TotalSpecificEnthalpy()
60 CeedScalar de_internal = gas.cv * ds.Y.temperature; in TotalSpecificEnthalpy_fwd()
70 Y.temperature = e_internal / gas.cv; in StatePrimitiveFromConservative()
86 dY.temperature = de_internal / gas.cv; in StatePrimitiveFromConservative_fwd()
94 const CeedScalar rho = Y.pressure / (GasConstant(gas) * Y.temperature); in StateEntropyFromPrimitive()
108 …rho = (dY.pressure * s.Y.temperature - s.Y.pressure * dY.temperature) / (GasConstant(gas) * s.Y.t… in StateEntropyFromPrimitive_fwd()
126 Y.temperature = -1 / (GasConstant(gas) * V.S_energy); in StatePrimitiveFromEntropy()
139 dY.temperature = dV.S_energy / (GasConstant(gas) * V.S_energy * V.S_energy); in StatePrimitiveFromEntropy_fwd()
150 U.density = Y.pressure / (GasConstant(gas) * Y.temperature); in StateConservativeFromPrimitive()
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H A Dtaylorgreen.h33 const CeedScalar density0 = reference.pressure / (reference.temperature * R); in ICsTaylorGreen()
44 Y[4] = reference.temperature; in ICsTaylorGreen()
H A Dbc_slip.h31 …lar Y_reflect[5] = {s.Y.pressure, vel_reflect[0], vel_reflect[1], vel_reflect[2], s.Y.temperature}; in Slip()
81 …lar Y_reflect[5] = {s.Y.pressure, vel_reflect[0], vel_reflect[1], vel_reflect[2], s.Y.temperature}; in Slip_Jacobian()
87 …_reflect[5] = {ds.Y.pressure, dvel_reflect[0], dvel_reflect[1], dvel_reflect[2], ds.Y.temperature}; in Slip_Jacobian()
H A Dbc_outflow.h57 y_ext.temperature = outflow->temperature; in RiemannOutflow()
131 y_ext.temperature = outflow->temperature; in RiemannOutflow_Jacobian()
133 dy_ext.temperature = 0; in RiemannOutflow_Jacobian()
H A Dbc_freestream_type.h20 CeedScalar temperature; member
H A Dblasius.h88 Y[4] = S_infty.Y.temperature * h[0]; in BlasiusSolution()
208 CeedScalar dE_internal = drho * gas.cv * S_infty.Y.temperature; in Blasius_Inflow_Jacobian()
211 dP = drho * Rd * S_infty.Y.temperature; // interior rho with exterior T in Blasius_Inflow_Jacobian()
H A Dnewtonian_types.h52 CeedScalar temperature; member
H A Dchannel.h113 const CeedScalar e_internal = gas.cv * s_exact.Y.temperature; in Channel_Inflow()
H A Ddifferential_filter.h47 v0[DIFF_FILTER_TEMPERATURE][i] = wdetJ * s.Y.temperature; in DifferentialFilter_RHS()
/honee/qfunctions/spanstats/ !
H A Dturbulence.h62 v[TURB_MEAN_DENSITY_TEMPERATURE][i] = wdetJ * s.U.density * s.Y.temperature; in ChildStatsCollection()
63 …v[TURB_MEAN_DENSITY_TEMPERATURE_FLUX_X][i] = wdetJ * s.U.density * s.Y.temperature * s.Y.velocity[… in ChildStatsCollection()
64 …v[TURB_MEAN_DENSITY_TEMPERATURE_FLUX_Y][i] = wdetJ * s.U.density * s.Y.temperature * s.Y.velocity[… in ChildStatsCollection()
65 …v[TURB_MEAN_DENSITY_TEMPERATURE_FLUX_Z][i] = wdetJ * s.U.density * s.Y.temperature * s.Y.velocity[… in ChildStatsCollection()
/honee/doc/ !
H A Dexamples.md22 … is default), which is a linear constant-pressure wave that transports temperature and transverse …
65 The domain is filled with an ideal gas at rest (zero velocity) with temperature 24.92 and pressure …
119 …defined in terms of the Exner pressure, $\pi(\bm{x},t)$, and potential temperature, $\theta(\bm{x}…
154 - Reference potential temperature
159 - Perturbation of potential temperature
189 where $H$ is the channel half-height, $u_{\max}$ is the center velocity, $T_w$ is the temperature a…
210 - Reference potential temperature
300 …rescribed by the Blasius soution profile, density is set constant, and temperature is allowed to f…
301 Using `weakT: true`, density is allowed to float and temperature is set constant.
321 - Freestream temperature
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H A Druntime_options.md242 - 1 Kelvin in scaled temperature units
351 These conditions may be either weak or strong, with the latter specifying velocity and temperature …
H A Dtheory.md20 … $\bm{g}$), $k$ the thermal conductivity constant, $T$ represents the temperature, and $P$ the pr…
325 …ile the middle three are linearly degenerate, carrying a contact wave (temperature) and transverse…
560 …forces velocity, with the option of weakly enforcing either density or temperature using the `-wea…