Maurice Tutor

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    Nov-2005 - Oct-2011

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    Phoniex University
    Oct-2001 - Nov-2016

Category > Management Posted 28 Sep 2017 My Price 6.00

heat transfer coefficient

7.7  Consider flow over a flat plate for which it is desired to determine the average heat transfer coefficient over the short span x1  to x2, h1-2, where (x2  - x1) � L.

 

ditions uoo and Too, in parallel flow over an isothermal                                         flat plate at Ts. Assuming that u = uoo  throughout the

thermal boundary layer, write the corresponding form of the boundary layer energy equation. Applying appropriate initial (x = 0) and boundary conditions, solve this equation for the boundary layer temperature

Ts

 

 

x                  x1   x2                  L

 

field, T(x, y). Use the result to obtain an expression for the local Nusselt number Nux. Hint: This problem is analogous to one-dimensional heat transfer in a semi- infinite medium with a sudden change in surface temperature.

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Maurice Tutor
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Status NEW Posted 28 Sep 2017 09:09 PM My Price 6.00

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