NOTE: Due to the relatively complex nature of
heat transfer, results gained from application of these
formulae, while useful, must be treated as approximations
only. Design safety margins should be considered before
final selection of any device.
1) Heat gained or
lost through the walls of an insulated container:
Where:
Q = Heat (Watts)
A = External surface area of container (m2)
DT = Temp. difference (inside
vs. outside of container) (Kelvin)
K = Thermal conductivity of insulation (Watt / meter Kelvin)
DX = Insulation thickness (m)
2) Time required to change the temperature
of an object:
Where:
t = Time interval (seconds)
m = Weight of the object (kg)
Cp= Specific heat of material (J / (kg K))
DT = Temperature change of object
(Kelvin)
Q = Heat added or removed (Watts)
NOTE:
It should be remembered that thermoelectric devices
do not add or remove heat at a constant rate when DT is
changing. An approximation for average Q is:
| Q ave =
(Q (DTmax) + Q (DTmin))
/ 2 |
3) Heat transferred to or from a surface
by convection:
Where:
Q = Heat (Watts)
h = Heat transfer coefficient (W / (m2 K))
(1 to 30 = "Free" convection - gases,
10 to 100 = "Forced" convection - gases)
A = Exposed surface area (m2)
DT = Surface Temperature - Ambient
(Kelvin)
Conversions:
Thermal
Conductivity |
1
BTU / hr ft °F = 1.73 W / m K |
| 1 W / m K = 0.578
BTU / hr ft °F |
Power
(heat flow rate) |
1
W = 3.412 BTU / hr |
| 1 BTU / hr = 0.293
W |
Area |
1
ft2 = 0.093 m2 |
| 1 m2
= 10.76 ft2 |
Length |
1
ft = 0.305 m |
| 1 m = 3.28 ft |
Specific
Heat |
1
BTU / lb °F = 4184 J / kg K |
| 1 J / kg K = 2.39
x 10-4 BTU / lb °F |
Heat
Transfer Coefficient |
1
BTU / hr ft2 °F = 5.677 W / m2
°K |
| 1 W / m2
°K = 0.176 BTU / hr ft2 °F |
Mass |
1
lb = 0.4536 kg |
| 1 kg = 2.205 lb
|
|