Conduction
Heat flows through a solid from hot to cold, at a rate set by the material's conductivity and the temperature gradient. This is Fourier's law:
q = −kdTdx
- q
- heat flux
- W/m²
- k
- thermal conductivity
- W/(m·K)
- T
- temperature
- K
- x
- distance through the material
- m
- Φ
- heat flow rate
- W
- A
- area
- m²
- L
- wall thickness
- m
- h
- convection coefficient
- W/(m²·K)
- ℓ
- pipe length
- m
- r
- radius
- m
| dT/dx | −200 K/m |
| q = k(T1 − T2)/L | 140 W/m² |
| Φ = qA | 1.4 kW |
Worked example
Uses the values in Fig. 2.1-1. Change them and the working updates.
Given
- kbrick0.7 W/(m·K)
- Lwall thickness100 mm
- Awall area10 m²
- T1hot face20 °C
- T2cold face0 °C
Find
The rate of heat flow Φ through the wall.
Solution
q = k(T1 − T2)/L = 0.7 W/(m·K) × (20 − 0) K / 0.1 m = 140 W/m²
Φ = qA = 140 W/m² × 10 m² = 1,400 W
Answer
Φ = 1.4 kW
Over 24 hours that is 33.6 kWh.
Related cases
-
Layers in series
Φ = A ΔTΣ(L/k)
-
Pipe wall
Φ = 2πkℓ ΔTln(r2/r1)
-
Convection at a surface
Φ = hA ΔT
Assumptions
- Conditions are steady: temperatures no longer change with time.
- Heat flows in one direction, straight through the wall. Edges and corners are ignored.
- k is constant over the temperature range, and no heat is generated inside the wall.
- The face temperatures are known. In practice the air films on each face add resistance, so use surface rather than room temperatures.
- Conductivities are typical values. Real figures vary with density, moisture and grade.
Derivation
- Fourier's law:
q = −k dT/dx. - In steady state with no heat generated, the same flux passes every plane, so q is constant through the wall.
- With k constant, dT/dx is constant too: the temperature falls linearly,
dT/dx = −(T1 − T2)/L. - So
q = k(T1 − T2)/L, and over area A,Φ = kA(T1 − T2)/L.
The minus sign in Fourier's law says heat flows down the temperature gradient, from hot to cold.