๐ 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.
โก Fortran 90 Engine
Double Precision (IEEE 754)
โ ISO / ASME Validated
๐ Solver Telemetry
โ ACTIVE
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โก Solves
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๐พ Downloads
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๐ฆ Fortran Code
10.8 KB
๐
Released
Jun 2026
โฑ๏ธ Latency
< 1 ms
๐ Enclosed Differentially Heated Cavity & Recirculation Roll
Real-time visual simulation of buoyant fluid rising along hot left wall and sinking along cold right wall๐ Configuration & Presets
๐ช Double Glazing Air Gap
โ๏ธ Solar Thermal Collector
โก Transformer Oil Channel
โข๏ธ Nuclear Containment Gap
Catton Enclosure Formulation:
โข Rayleigh Number: RaW = [ g ฮฒ (Th โ Tc) Wยณ ] / (ฮฝ ฮฑ)
โข Average Nusselt: Nu = 0.22 ยท [ RaW Pr / (0.2 + Pr) ]0.28 ยท (H/W)โ0.25
โข Heat Rate: Qฬ = Nu ยท (k / W) ยท (H ยท L) ยท (Th โ Tc) [W]
โข Boundary Layer Thickness: ฮด โ W ยท RaWโ1/4
โข Rayleigh Number: RaW = [ g ฮฒ (Th โ Tc) Wยณ ] / (ฮฝ ฮฑ)
โข Average Nusselt: Nu = 0.22 ยท [ RaW Pr / (0.2 + Pr) ]0.28 ยท (H/W)โ0.25
โข Heat Rate: Qฬ = Nu ยท (k / W) ยท (H ยท L) ยท (Th โ Tc) [W]
โข Boundary Layer Thickness: ฮด โ W ยท RaWโ1/4
๐ Cavity Convection Results
๐ Output Summary
Total Convective Heat Rate (Qฬ)
Qฬ = 6.55 kW
Average HTC: 1.46 W/(mยฒยทK) | Nuavg = 12.13
RaW = 5.73e+7
Cavity Rayleigh (RaW)
5.73e+7
Boundary layer regime
Enclosure Aspect Ratio (A = H/W)
40.0
Prandtl Pr = 0.71
Wall BL Thickness (ฮด)
2.87 mm
Boundary layer scale
Max Buoyant Velocity
5.033 m/s
โ(g ฮฒ ฮT H)
๐ Average Nusselt Nu vs Cavity Spacing W (mm)
๐ Heat Transfer Rate Qฬ (W) vs Temperature Difference ฮT (ยฐC)
================================================================= THERMOFLUIDCALC โ CAVITY NATURAL CONVECTION (CATTON MODEL) REPORT ================================================================= Case Title : Nuclear Containment Passive Safety Air Annulus Gap Cavity Dimensions : Height H = 10.00 m, Spacing W = 0.2500 m, Depth L = 5.00 m (Aspect A = 40.0) Wall Temperatures : Hot Th = 120.0 C, Cold Tc = 30.0 C (DeltaT = 90.0 C) Rayleigh Number (Ra_W) : 5.727e+7 Prandtl Number (Pr) : 0.707 ----------------------------------------------------------------- AVERAGE NUSSELT (Nu_avg) : 12.129 Heat Transfer Coeff (h_avg): 1.46 W/(m2.K) TOTAL HEAT TRANSFER RATE Q : 6549.66 W (6.550 kW) BL Thickness (delta_bl) : 2.87 mm Maximum Buoyant Velocity : 5.033 m/s =================================================================
๐ Calculation Methodology & Cavity Convection Standards
Catton & Berkovsky-Polevikov Model
Natural convection in differentially heated tall enclosures transitions through three regimes based on $Ra_W$:
โข Ra < 10ยณ: Conduction ($Nu = 1$)
โข 10โด ≤ Ra ≤ 10โท: $Nu = 0.22 (Ra Pr / (0.2+Pr))^{0.28} A^{-0.25}$
โข 10โด ≤ Ra ≤ 10โท: $Nu = 0.22 (Ra Pr / (0.2+Pr))^{0.28} A^{-0.25}$
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 $Ra_W \approx 10^7$.