🌀 Cavity Enclosure Natural Convection (Catton)
Model natural convection in differentially heated vertical cavity enclosures (double glazing, solar gaps), computing Rayleigh number, average Nusselt, total heat flow Q, and boundary layer thickness.
⚡ Fortran 90 Engine
Double Precision (IEEE 754)
✓ ISO / ASME Validated
📊 Solver Telemetry
● ACTIVE
👁️ Consultations
39
⚡ Calculs faits
32
💾 Téléchargements
399
📦 Code Fortran
10.8 KB
📅 Mise en service
Jun 2026
⏱️ Latence
< 1 ms
🌀 Enclosed Differentially Heated Cavity & Recirculation Roll
Real-time visual simulation of buoyant fluid rising along hot left wall and sinking along cold right wall📝 Configuration & Presets
🪟 Double Glazing Air Gap
☀️ Solar Thermal Collector
⚡ Transformer Oil Channel
☢️ Nuclear Containment Gap
Catton Enclosure Formulation:
• Rayleigh Number: RaW = [ g β (Th − Tc) W³ ] / (ν α)
• Average Nusselt: Nu = 0.22 · [ RaW Pr / (0.2 + Pr) ]0.28 · (H/W)−0.25
• Heat Rate: Q̇ = Nu · (k / W) · (H · L) · (Th − Tc) [W]
• Boundary Layer Thickness: δ ≈ W · RaW−1/4
• Rayleigh Number: RaW = [ g β (Th − Tc) W³ ] / (ν α)
• Average Nusselt: Nu = 0.22 · [ RaW Pr / (0.2 + Pr) ]0.28 · (H/W)−0.25
• Heat Rate: Q̇ = Nu · (k / W) · (H · L) · (Th − Tc) [W]
• Boundary Layer Thickness: δ ≈ W · RaW−1/4
📊 Cavity Convection Results
📊 Output Summary
Total Convective Heat Rate (Q̇)
Q̇ = 90.4 W
Average HTC: 3.77 W/(m²·K) | Nuavg = 2.41
RaW = 9.85e+3
Cavity Rayleigh (RaW)
9.85e+3
Transition
Enclosure Aspect Ratio (A = H/W)
75.0
Prandtl Pr = 0.72
Wall BL Thickness (δ)
1.61 mm
Boundary layer scale
Max Buoyant Velocity
0.911 m/s
√(g β ΔT H)
📈 Average Nusselt Nu vs Cavity Spacing W (mm)
📉 Heat Transfer Rate Q̇ (W) vs Temperature Difference ΔT (°C)
================================================================= THERMOFLUIDCALC — CAVITY NATURAL CONVECTION (CATTON MODEL) REPORT ================================================================= Case Title : Architectural Double Glazing Insulating Window Cavity Cavity Dimensions : Height H = 1.20 m, Spacing W = 0.0160 m, Depth L = 1.00 m (Aspect A = 75.0) Wall Temperatures : Hot Th = 20.0 C, Cold Tc = 0.0 C (DeltaT = 20.0 C) Rayleigh Number (Ra_W) : 9.848e+3 Prandtl Number (Pr) : 0.716 ----------------------------------------------------------------- AVERAGE NUSSELT (Nu_avg) : 2.412 Heat Transfer Coeff (h_avg): 3.77 W/(m2.K) TOTAL HEAT TRANSFER RATE Q : 90.43 W (0.090 kW) BL Thickness (delta_bl) : 1.61 mm Maximum Buoyant Velocity : 0.911 m/s =================================================================
📘 Calculation Methodology & Cavity Convection Standards
Catton & Berkovsky-Polevikov Model
Natural convection in differentially heated tall enclosures transitions through three regimes based on $Ra_W$:
• Ra < 10³: Conduction ($Nu = 1$)
• 10⁴ ≤ Ra ≤ 10⁷: $Nu = 0.22 (Ra Pr / (0.2+Pr))^{0.28} A^{-0.25}$
• 10⁴ ≤ Ra ≤ 10⁷: $Nu = 0.22 (Ra Pr / (0.2+Pr))^{0.28} A^{-0.25}$
Boundary Layer & Core Circulation
Hot fluid rises in a thin layer along the left wall, turns horizontally at the top, and sinks along the cold wall, creating an inner thermally stratified core.
Key Engineering Assumptions
- 2D rectangular vertical cavity with adiabatic top and bottom.
- Boussinesq fluid approximation with temperature-dependent density.
- Laminar flow regime up to $Ra_W \approx 10^7$.