19.6 Consider a compressible, laminar boundary layer over a flat plate. Assuming Pr = 1 and a calorically perfect gas, show that the profile of total temperature through the boundary layer is a function of the velocity profile via To = Tw + (To,e – T)- where Tw = wall temperature and To,e and u̟ are the total temperature and velocity, respectively, at the outer edge of the boundary layer. [Hint:

19.6 Consider a compressible, laminar boundary layer over a flat plate. Assuming Pr = 1 and a calorically perfect gas, show that the profile of total temperature through the boundary layer is a function of the velocity profile via To = Tw + (To,e – T)- where Tw = wall temperature and To,e and u̟ are the total temperature and velocity, respectively, at the outer edge of the boundary layer. [Hint:

Principles of Heat Transfer (Activate Learning with these NEW titles from Engineering!)

8th Edition

ISBN:9781305387102

Author:Kreith, Frank; Manglik, Raj M.

Publisher:Kreith, Frank; Manglik, Raj M.

Chapter5: Analysis Of Convection Heat Transfer

Section: Chapter Questions

Problem 5.44P

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