🧊 2D Transient Conduction & Heisler Multi-D

Calculate 2D multidimensional transient heat conduction in rectangular billets: center core temperature (T0), corner surface temperature, Biot and Fourier numbers, and heat removed (Q/Qmax).

⚡ Fortran 90 Engine Double Precision (IEEE 754) ✓ ISO / ASME Validated
📊 Solver Telemetry ● ACTIVE
👁️ Consultations 22
⚡ Calculs faits 21
💾 Téléchargements 321 📦 Code Fortran 3.4 KB
📅 Mise en service Jun 2026
⏱️ Latence < 1 ms
⚡ Outils & Rapports :
💾 Télécharger Fortran 90

🧊 2D Rectangular Billet Quenching & Isothermal Contour Field

Real-time visual simulation of internal heat diffusion migrating from center core to convective boundaries

📝 Configuration & Presets

🔩 Steel Billet Water Quench 🪟 Aluminum Extrusion Air Cool 🧱 Ceramic Furnace Lining 💻 Silicon CPU Die Surge
📐 Geometry (Half-Widths)
Total 2Lx = 60 mm
Total 2Ly = 120 mm
🧪 Material Physical Properties
🌡️ Thermal Boundary Conditions
2D Heisler Product Formulation:
• Dimensionless Temp: θ(x,y,t) = θx(x,t) · θy(y,t)
• Center Solution: θ₀ = [ Cx e−ζx² Fox ] · [ Cy e−ζy² Foy ]
• Transcendental Roots: ζ · tan(ζ) = Bi
• Heat Removed: Q / Qmax = 1 − θ₀ · (sin ζx sin ζy) / (ζx ζy)

📊 Transient Conduction Results

📊 Output Summary
💾 Fortran Source

Center Core Temperature (T₀)
T₀ = 421.2 °C (θ = 0.8341)
Corner Temp: 417.3 °C | Energy Removed: 16.9 %
t = 180.0 s
Biot Numbers (Bix / Biy) 0.010 / 0.020 Lumped regime
Fourier Numbers (Fox / Foy) 14.815 / 3.704 Dimensionless times
Thermal Diffusivity (α) 7.41e-5 m²/s k / (ρ · cp)
Corner Surface Temperature 417.3 °C Fastest cooled point

📈 Center & Corner Temperature (°C) vs Time (s)

📉 Fraction of Thermal Energy Transferred Q/Q_max (%)

=================================================================
 THERMOFLUIDCALC — 2D TRANSIENT CONDUCTION REPORT
=================================================================
Case Title                 : Aluminum Alloy Extrusion Profile Forced Air Cooling
Billet Dimensions          : 2Lx = 60.0 mm, 2Ly = 120.0 mm
Thermophysical Properties  : k = 180.00 W/m.K, rho = 2700.0 kg/m3, cp = 900.0 J/kg.K (alpha = 7.407e-5 m2/s)
Thermal Conditions         : Ti = 500.0 C, Tinf = 25.0 C, h = 60.0 W/m2.K, t = 180.0 s
-----------------------------------------------------------------
Biot Numbers (Bix / Biy)   : 0.0100 / 0.0200
Fourier Numbers (Fox / Foy): 14.8148 / 3.7037
CENTER CORE TEMPERATURE T0 : 421.21 deg C (theta = 0.8341)
CORNER TEMPERATURE T_corn  : 417.27 deg C (theta = 0.8258)
Energy Transferred (Q/Qmax): 16.86 %
=================================================================

📘 Calculation Methodology & Multidimensional Heisler Standards

Heisler Product Theorem

For multidimensional geometric solids (infinite rectangular bar), the dimensionless temperature is the direct product of 1D infinite slab analytical solutions:

θ(x,y,t) = θslab,x(x,t) × θslab,y(y,t)

Spatial Temperature Distribution

The corner cools first due to simultaneous two-sided convective exposure ($\theta_{corner} = \theta_{surf,x} \cdot \theta_{surf,y}$), while the core retains thermal energy.

Key Engineering Assumptions

  • Homogeneous, isotropic solid with constant thermal diffusivity $\alpha$.
  • Uniform initial temperature $T_i$ and uniform ambient quench convection $h$.
  • Fourier numbers $Fo > 0.2$ for high-accuracy single-term series representation.