Calculation inputs Requirements pending The equation is recorded. Required inputs, regimes and validity limits will be added next. Inlet temperature °CK°F Outlet temperature °CK°F Absolute pressure kPaPabarpsi Flow velocity m/sft/s Plate length mmmcmin Calculate HTC → Inlet temperature °CK°F Outlet temperature °CK°F Absolute pressure kPaPabarpsi Free-stream velocity m/sft/s Leading-edge cylinder diameter (D) mmmcmin Angular position from stagnation point (θ) degrad Inner-cylinder radius (r_i) mmmcmin Radial clearance (Δr) mmmcmin Inner-cylinder rotational speed (ω) rpmrad/s T_bulk and T_solid are calculated automatically. Table 3-3 air properties, Reynolds number and Prandtl number are derived from the entered state. Calculate HTC → Inlet temperature °CK°F Outlet temperature °CK°F Absolute pressure kPaPabarpsi Rotational speed (omega) rpmrad/s Local radius mmmcmin Temperature-distribution exponent (n) Core swirl ratio (XK) Flow regime Automatic from Reynolds number Laminar Turbulent T_bulk = (T_in + T_out)/2 and T_solid = 0.95 T_bulk are calculated automatically. Calculate HTC → Inlet temperature °CK°F Outlet temperature °CK°F Absolute pressure kPaPabarpsi Mass flow rate (ṁ) kg/sg/slb/s Duct diameter (D) mmmcmin Hydraulic diameter (D_h) mmmcmin Flow cross-sectional area (A) mm²cm²m²in² Heated duct length (L) mmmcmin Inner diameter (D_i) mmmcmin Outer diameter (D_o) mmmcmin Darcy friction factor (f) Heat-transfer wall Inner wall heated/cooled Outer wall heated/cooled Mean velocity is calculated automatically from V = ṁ/(ρA). For methods 2.4 and 2.5, enter the actual flow area because hydraulic diameter alone does not define it. T_bulk, T_solid, air properties, Prandtl and Reynolds are derived automatically. Methods 2.4–2.6 require the Darcy—not Fanning—friction factor. Calculate HTC → Inlet fluid temperature °CK°F Outlet fluid temperature °CK°F Absolute pressure kPaPabarpsi Surface height (L) mmmcmin T_bulk = (T_in + T_out)/2, T_solid = 0.95 T_bulk and T_film = (T_bulk + T_solid)/2 are calculated automatically. Air properties, beta, Gr_L, Pr and Ra_L are evaluated automatically. Calculate HTC → Inlet temperature °CK°F Outlet temperature °CK°F Absolute pressure kPaPabarpsi Rotational speed (omega) rpmrad/s Local radius (r) mmmcmin Surface/cone half-angle (theta) degrad Leakage mass-flow rate (W) g/skg/slb/s Number of seal teeth (N) T_bulk = (T_in + T_out)/2 and T_solid = 0.95 T_bulk are calculated automatically. Density and, for 6.1, viscosity and Re_omega are derived automatically. Calculate windage heat flux → Mainstream hot-gas temperature (T_∞) °CK°F Coolant supply temperature (T_2) °CK°F Mainstream absolute pressure (P_∞) kPaPabarpsi Coolant absolute pressure (P_2) kPaPabarpsi Mainstream velocity (U_∞) m/sft/s Coolant injection velocity (U_2) m/sft/s Slot height (s) mmmcmin Distance downstream from injection (x) mmmcmin Actual wall temperature (T_w) °CK°F Air–air model: density, viscosity, c_p, mass-velocity ratio M_s and coolant Reynolds number Re_2 are calculated automatically. T_bulk and T_solid are not used. Calculate film conditions → Upstream absolute pressure (P_i) kPaPabarpsi Downstream absolute pressure (P_e) kPaPabarpsi Minimum flow area (A) mm²cm²m²in² Inlet total temperature (T_i) °CK°F Specific gas constant (R) J/kg·K Discharge coefficient (C_dh) Specific-heat ratio (γ) Discharge coefficient (C_D) Fluid density (ρ) kg/m³ Pressure ratio and the labyrinth flow function are calculated automatically. Use absolute—not gauge—pressures. No T_bulk or T_solid value is used in this section. Calculate mass flow →