Module 5.05 - Forced Connection Through Circular Pipe
Data
Density, ρ = 62.00 lb/ft3
Viscosity, μ = 1.65 lb/(ft·hr)
Thermal Conductivity, k; = 0.36 Btu/(hr·ft·°F)
Heat Capacity, c = 1.00 Btu/(lb·°F)
Inside Diameter, d = 1.33 in
Tube Length, L; = 10.00 ft
Viscosity at Wall Temperature, μw = 1.41 lb/(ft·hr)
Viscosity Correction Factor, φi = 0.00
Mass Flow Rate, w = 10000.00 lb/hr
Area, a = 0.01 ft2
Velocity, V = 16617.64 ft/hr
Reynold Number, Re = 69415
Prandtl Number, Pr = 4.54
Graetz Number, Gz = 3501
Case 4.
Nu =0.023·Re⅘·Pr⅓·φi
Nusselt Number, Nu = 290.60
hi=k·Nu/d
Inside film coefficient, hi = 948.93 Btu/(hr·ft2·°F)