Natural Convection Correlations: enclosed_cavity_vertical

Nusselt number correlations for natural (free) convection heat transfer. Covers vertical plates, horizontal plates (hot side up/down), horizontal cylinders, vertical cylinders, spheres, inclined plates, and enclosed cavities (vertical and horizontal). Each record provides the Nu correlation equation, valid Rayleigh number range, C and n coefficients (for power-law forms), characteristic length definition, Prandtl number range, and source reference. 30 records spanning all standard geometries from Churchill-Chu, Morgan, McAdams, Globe-Dropkin, Berkovsky-Efimov, Catton, and Hollands correlations.

Mechanical Engineeringgeometry: enclosed_cavity_vertical3 rows
geometrycorrelation idNu correlation textPr range max (dimensionless)Pr range min (dimensionless)Ra max (dimensionless)Ra min (dimensionless)characteristic length definitionfluid assumptionorientationsource author
enclosed_cavity_verticalBerkovsky & Efimov (1977) mid-Ra#1e3-1e7Nu = 0.22*(Ra*Pr/(0.2+Pr))^0.28*(H/L)^(-0.25)400.110,000,0001,000L = cavity gap width; H/L = 2-10 (aspect ratio); Pr=0.1-40any fluidvertical cavity (side-heated) H/L=2-10Berkovsky & Efimov (1977) mid-Ra
enclosed_cavity_verticalBerkovsky & Efimov (1977) square#1e1-1e5Nu = 0.18*(Ra*Pr/(0.2+Pr))^0.29400.1100,00010L = cavity gap; H/L near 1 (square cavity); Pr=0.1-40any fluidvertical square cavity H/L=1Berkovsky & Efimov (1977) square
enclosed_cavity_verticalCatton (1978) conduction#1-1e3Nu = 1 (pure conduction; no convection)500.51,0001L = cavity gap width; Ra < 1000: viscous forces prevent circulationair (Pr~0.7)vertical cavity (side-heated) conduction limitCatton (1978) conduction

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