HEAT TRANSFER | ||
With the cooperation and under supervision of our past president Ir. H. Ghys | ||
In practice heat transfer is the sum of the heat transfer that takes place through conductivity, convection and radiation. The relation below applies: | ||
q = k x A x∆T x t | ||
q : The quantity of heat ( j )
k : total heat transfer coeff. ( W/m2 x K) |
A : area (m2)
∆T = temperature difference |
t : time ( s ) |
Heat transfer frequently occurs between two bodies,
separated by a wall.
For such a (clean) flat wall the relation below applies: |
||
1/k = 1/α1 + d/λ + 1/α2 | ||
k : total heat transfer coeff. ( W/m2
x K)
α = heat transfer coefficient on respective sides of the wall ( W/m2 x K ) |
d = thickness of the wall ( m ) | λ = coefficient of thermal conductivity for the wall (W/m x K) |
The transferred quantity of heat in a heat exchanger, is at each point a function of the prevailing heat difference and the total heat transfer coefficient. Applicable to the entire heat transfer surface is: | ||
Q = k x A x LMTD | ||
Q = tranferred quantity oh heat ( Watt )
k = total heat transfer coeff. (W/m2 x K) |
A = heat transferring surface (m2) | LMTD = logarithmic mean temperature diff. ( K ) |
The logarithmic mean temperature difference is defined as the relation between the temperature difference at the heat exchanger's two connection sides according to the expression: | ||
LMTD = (Δ1- Δ2 / ( In Δ1 / Δ2 ) | ||
LMTD = logarithmic mean tempt. diff.(K) | Δ1 = the tempt. difference ( K ) | Δ2 = the temperature difference ( °K ) |