Forced Convection Correlations: noncircular_cylinder

Nusselt number correlation constants for forced convection heat transfer. Covers external cross-flow over cylinders (Hilpert circular, noncircular shapes, Zukauskas), tube bank arrays (C1/m constants and C2 row correction factors), and fully developed laminar internal flow in noncircular ducts. Each record provides C and m coefficients for power-law Nu correlations, valid Reynolds number range, and source reference. 51 records from Incropera Chapter 7 (Tables 7.2-7.6) and Chapter 8 (Table 8.1).

Mechanical Engineeringcorrelation_type: noncircular_cylinder3 rows
correlation typecorrelation subtypeC (dimensionless)Nu correlation textRe max (dimensionless)Re min (dimensionless)conditionsgeometry descriptionm (dimensionless)
noncircular_cylinderhexagon_flat0.15Nu = C * Re_D^m * Pr^(1/3)90,7004,500External cross-flow; properties at film temp T_f; Pr >= 0.7Hexagonal cylinder flat face facing flow0.638
noncircular_cylinderhexagon_pointy_high_Re0.039Nu = C * Re_D^m * Pr^(1/3)105,00020,400External cross-flow; properties at film temp T_f; Pr >= 0.7Hexagonal cylinder point facing flow (Re 20400-105000)0.78
noncircular_cylinderhexagon_pointy_low_Re0.164Nu = C * Re_D^m * Pr^(1/3)20,4005,200External cross-flow; properties at film temp T_f; Pr >= 0.7Hexagonal cylinder point facing flow (Re 5200-20400)0.638

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