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ADWallHeatTransferCoefficientGnielinskiMaterial.C
Go to the documentation of this file.
1//* This file is part of the MOOSE framework
2//* https://mooseframework.inl.gov
3//*
4//* All rights reserved, see COPYRIGHT for full restrictions
5//* https://github.com/idaholab/moose/blob/master/COPYRIGHT
6//*
7//* Licensed under LGPL 2.1, please see LICENSE for details
8//* https://www.gnu.org/licenses/lgpl-2.1.html
9
13#include "Numerics.h"
14
16
19{
21 params.addParam<MaterialPropertyName>("Hw",
23 "Heat transfer coefficient material property");
24 params.addParam<MaterialPropertyName>(
25 "rho", FlowModelSinglePhase::DENSITY, "Density of the fluid");
26 params.addParam<MaterialPropertyName>("vel", FlowModelSinglePhase::VELOCITY, "Fluid velocity");
27 params.addParam<MaterialPropertyName>(
28 "D_h", FlowModelSinglePhase::HYDRAULIC_DIAMETER, "Hydraulic diameter");
29 params.addParam<MaterialPropertyName>(
30 "cp", FlowModelSinglePhase::SPECIFIC_HEAT_CONSTANT_PRESSURE, "Specific heat of the fluid");
31 params.addParam<MaterialPropertyName>(
32 "mu", FlowModelSinglePhase::DYNAMIC_VISCOSITY, "Dynamic viscosity of the fluid");
33 params.addParam<MaterialPropertyName>(
34 "k", FlowModelSinglePhase::THERMAL_CONDUCTIVITY, "Heat conductivity of the fluid");
35 params.addParam<MaterialPropertyName>(
36 "T", FlowModelSinglePhase::TEMPERATURE, "Fluid temperature");
37 params.addParam<MaterialPropertyName>("T_wall", FlowModel::TEMPERATURE_WALL, "Wall temperature");
38 params.addClassDescription("Computes wall heat transfer coefficient for gases and water using "
39 "the Gnielinski correlation");
40 return params;
41}
42
44 const InputParameters & parameters)
45 : Material(parameters),
46 _Hw(declareADProperty<Real>("Hw")),
47 _rho(getADMaterialProperty<Real>("rho")),
48 _vel(getADMaterialProperty<Real>("vel")),
49 _D_h(getADMaterialProperty<Real>("D_h")),
50 _k(getADMaterialProperty<Real>("k")),
51 _mu(getADMaterialProperty<Real>("mu")),
52 _cp(getADMaterialProperty<Real>("cp")),
53 _T(getADMaterialProperty<Real>("T")),
54 _T_wall(getADMaterialProperty<Real>("T_wall"))
55{
56}
57
58void
60{
61 using std::max, std::sqrt, std::pow, std::log10;
62
64 ADReal Re = max(1.0, THM::Reynolds(1., _rho[_qp], _vel[_qp], _D_h[_qp], _mu[_qp]));
65
66 if (Re < 2300 || Re > 5E+6 || Pr < 0.5 || Pr > 2000)
67 {
68 mooseDoOnce(mooseWarning(
69 "The Gnielinski correlation is valid when Pr is between 0.5 and 2000, and Re is "
70 "between 2300 and 5000000. Be aware that using values out of this range may lead to "
71 "significant errors in your results!"));
72 }
73
74 ADReal f = pow(1.82 * log10(Re) - 1.64, -2.0);
75 ADReal Nu = ((f / 8.0) * max(0.0, Re - 1000.0) * Pr) /
76 (1.0 + 12.7 * sqrt(f / 8.0) * (pow(Pr, 2.0 / 3.0) - 1.0));
77 _Hw[_qp] = THM::wallHeatTransferCoefficient(Nu, _k[_qp], _D_h[_qp]);
78}
DualNumber< Real, DNDerivativeType, true > ADReal
registerMooseObject("ThermalHydraulicsApp", ADWallHeatTransferCoefficientGnielinskiMaterial)
Real f(Real x)
Test function for Brents method.
ExpressionBuilder::EBTerm pow(const ExpressionBuilder::EBTerm &left, T exponent)
const double Re
Computes wall heat transfer coefficient for gases and water using the Gnielinski correlation.
const ADMaterialProperty< Real > & _cp
Specific heat capacity.
const ADMaterialProperty< Real > & _k
Thermal conductivity.
ADMaterialProperty< Real > & _Hw
Wall heat transfer coefficient.
static const std::string DENSITY
static const std::string HYDRAULIC_DIAMETER
static const std::string VELOCITY
static const std::string HEAT_TRANSFER_COEFFICIENT_WALL
static const std::string DYNAMIC_VISCOSITY
static const std::string SPECIFIC_HEAT_CONSTANT_PRESSURE
static const std::string THERMAL_CONDUCTIVITY
static const std::string TEMPERATURE
static const std::string TEMPERATURE_WALL
Definition FlowModel.h:108
void addParam(const std::string &name, const std::initializer_list< typename T::value_type > &value, const std::string &doc_string)
void addClassDescription(const std::string &doc_string)
unsigned int _qp
static InputParameters validParams()
void mooseWarning(Args &&... args) const
auto Prandtl(const T1 &cp, const T2 &mu, const T3 &k)
Compute Prandtl number.
Definition Numerics.h:133
auto Reynolds(const T1 &volume_fraction, const T2 &rho, const T3 &vel, const T4 &D_h, const T5 &mu)
Compute Reynolds number.
Definition Numerics.h:118