Flow Over Heated Plate

Classical conjugate heat transfer validation case with a heated flat plate (Vynnycky et al.).

Repository path: tutorials/conjugateHeatTransfer/flowOverHeatedPlate

Reference: Alkafri et al. (2024), multiRegionFoam: A Unified Multiphysics Framework, Sect. 7.1

Overview

An incompressible laminar flow over a flat plate of finite thickness is considered. A fluid of uniform temperature $T_\infty = 300\,\text{K}$ and velocity $U_\infty = 1\,\text{m/s}$ flows over a plate of length $L = 1\,\text{m}$ held at a constant bottom temperature $T_s = 310\,\text{K}$.

The aspect ratio is fixed at $\lambda = a/L = 0.25$. Results are validated against the numerical and analytical reference solutions from Vynnycky et al., computing the dimensionless conjugate boundary temperature

$$\theta = \frac{T - T_\infty}{T_s - T_\infty}.$$

Computational domain

Fig. 7 — Computational domain and boundary conditions for the flow over a heated plate.

Fig. 7 — Computational domain and boundary conditions for the flow over a heated plate.

Boundary conditions

Table: General boundary conditions

BoundaryThermalVelocity
Fluid
inlet300 K(1 0 0)ᵀ m/s
bottom (no-slip, plate)coupled(0 0 0)ᵀ m/s
slip-bottom (before plate)zeroGradientzeroGradient
outlet, topzeroGradientzeroGradient
Solid
topcoupled
bottom310 K
left, rightzeroGradient

Table: Coupled thermal boundary conditions at the fluid–solid interface

RegionBoundaryPartitionedMonolithic
FluidbottomregionCoupledTemperatureJumpmonolithicTemperature
SolidtopregionCoupledHeatFluxmonolithicTemperature

Material properties

Table: Thermophysical properties of fluid and solid

PropertySymbolUnitSolidFluid
Densityρkg/m³11
Dynamic viscosityμkg/msρ_f U∞ L / Re
Thermal conductivitykW/m·K100k_s / k
Specific heat capacityc_pJ/kg·K100k_f Pr / μ

Mesh

Fig. 8 — Meshes for the flow over a heated plate simulation. Both fluid and solid regions use hexahedral elements with mesh grading towards the fluid–solid interface.

Fig. 8 — Meshes for the flow over a heated plate simulation. Both fluid and solid regions use hexahedral elements with mesh grading towards the fluid–solid interface.

Parameter study

Table: Simulated parameter combinations

RePrk
5000.011, 5, 20
10 0000.011, 5, 20
5001001, 5, 20

Simulations are run for 10 s with a time step $\Delta t = 0.01\,\text{s}$.

Numerical schemes

Table: Numerical schemes

SchemeSetting
ddtSchemebackward
gradSchemeleastSquares
divScheme div(phi,U)Gauss upwind
divScheme div(phi,T)Gauss linearUpwind Gauss linear
laplacianSchemeGauss linear corrected
interpolationSchemelinear
snGradSchemecorrected

Results summary

Fig. 9 — Simulation results for different Pr, Re, and k values. (a) θ for Pr=0.01, Re=500. (b) θ for Pr=0.01, Re=10⁴. (c) θ for Pr=100, Re=500. (d) Average coupling time for partitioned (Aitken) and monolithic coupling.

Fig. 9 — Simulation results for different Pr, Re, and k values. (a) θ for Pr=0.01, Re=500. (b) θ for Pr=0.01, Re=10⁴. (c) θ for Pr=100, Re=500. (d) Average coupling time for partitioned (Aitken) and monolithic coupling.

Both monolithic and partitioned (Aitken relaxation) coupling reproduce the reference solutions from Vynnycky et al. for all Pr, Re, and k combinations. Monolithic coupling exhibits lower or equal average coupling time compared to partitioned coupling across all cases, with the most notable advantage at Pr = 100 where monolithic coupling time is nearly constant.

Running the case

cd $FOAM_RUN/../multiPhysicsFoam/tutorials/conjugateHeatTransfer/flowOverHeatedPlate

# Partitioned coupling — serial
./Allrun --partitioned --serial

# Partitioned coupling — parallel
./Allrun --partitioned --parallel