Consider a concentric tube heat exchanger. Assuming there is no fin attached to any of the surfaces and considering negligible fouling, what would be the appropriate equation for calculating the overall heat transfer coefficient?

Respuesta :

Answer:

[tex]Q = T1 - T2 (KA)/L[/tex]

Explanation:

Where Q is the co-efficient of heat transfer.

T-1 is initial temperature of exchanger

T-2 is final temperature of sink where has to to be dissipated

k is the co-efficient of thermal conductivity

A is the total area of exchanger surface...

and L is the total length of exchanger...