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The
general equation for heat transfer across a surface is:
Q = UA
Δtm
(eq – 1.7)
Where Q
= heat transferred per unit time (W)
U = the overall heat transfer coefficient (W/m2 oC)
A –heat-transfer area, m2,
Δtm = the mean temperature difference, the temperature
driving force, oC.
The
overall coefficient is the reciprocal of the overall resistance to heat
transfer, which is the sum of several individual resistances, is given by:
1
= 1 + 1 + (doIn(do/di))
+ do >< 1 + do >< 1
(eq – 1.8)
Uo ho hod
2kw di hid di
hi
Where
Uo = the overall coefficient based on the outside area of the tube,
W/m2 oC,
ho = outside fluid film coefficient, W/m2 oC,
hi = inside fluid film coefficent, W/m2 oC,
hod = outside dirt coefficient (fouling factor), W/m2
oC,
hid = inside dirt coefficient, W/m2 oC,
kw = thermal conductivity of the tube wall material, W/m2
oC,
di = tube inside diameter, m,
do= tube outside diameter, m.
The
magnitude of the individual coefficients will depend on the nature of the
transfer process (conduction, convection, condensation, boiling or radiation),
on the physical properties of fluids, on the fluid flow-rates, and on the
physical arrangement of the heat transfer surface.
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Introduction |
Combined heat transfer process |
Heat transfer in cooling tower |
Variables affecting performance of CT heat transfer |
Heat transfer within
cooling system (heat exchanger) |
Types of heat exchanger |
Basic design
procedure and theory |
Designing a test heat exchanger |
Log Mean Temperature
difference | L.M.T.D. Correction factors |
Overall heat transfer coefficient |
Elaborated method for calculating U values |
Effect of scale formation |
Condensation of steam |
Condenser, where the hot fluid temperature varies |
Significance of pressure |
Significance of flow rate |
Methods of checking steam
condenser performance |
Common conversion factors
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