🧊 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
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3.4 KB
📅 Mise en service
Jun 2026
⏱️ Latence
< 1 ms
🧊 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
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)
• 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
Center Core Temperature (T₀)
T₀ = 549.8 °C (θ = 0.6339)
Corner Temp: 393.0 °C | Energy Removed: 43.4 %
t = 300.0 s
Biot Numbers (Bix / Biy)
0.500 / 0.800
Spatial gradients active
Fourier Numbers (Fox / Foy)
1.433 / 0.560
Dimensionless times
Thermal Diffusivity (α)
1.19e-5 m²/s
k / (ρ · cp)
Corner Surface Temperature
393.0 °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 : Structural Carbon Steel Billet Water Quenching Billet Dimensions : 2Lx = 100.0 mm, 2Ly = 160.0 mm Thermophysical Properties : k = 45.00 W/m.K, rho = 7850.0 kg/m3, cp = 480.0 J/kg.K (alpha = 1.194e-5 m2/s) Thermal Conditions : Ti = 850.0 C, Tinf = 30.0 C, h = 450.0 W/m2.K, t = 300.0 s ----------------------------------------------------------------- Biot Numbers (Bix / Biy) : 0.5000 / 0.8000 Fourier Numbers (Fox / Foy): 1.4331 / 0.5598 CENTER CORE TEMPERATURE T0 : 549.79 deg C (theta = 0.6339) CORNER TEMPERATURE T_corn : 393.04 deg C (theta = 0.4427) Energy Transferred (Q/Qmax): 43.39 % =================================================================
📘 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.