Thermal conduction through layered materials
Analyse steady thermal conduction through layered slabs and cylindrical insulation using thermal-resistance methods.
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ContinueThis page gives the UY1 working model/result for Thermal conduction through a compound slab. You reuse it when you turn thermal intuition into calculable models (energy balances, process reasoning, and kinetic/statistical links), with careful sign/units checks.
- Module path: Thermodynamics (UY1)
- Full routing: UY1 assessment map
- Math toolkit: Mathematics for undergraduate physics
At a glance
- Prerequisites: Fourier law for a single slab, steady-state heat flow.
- Outcomes: solve multilayer slab and cylindrical insulation conduction.
- Key result: thermal resistances in series add directly.
- Common trap: assuming temperature drops equally across layers with different k and L.
Setup
Steady 1D conduction through two layers in series:
- Same area A.
- Layer 1: (k₁,L₁), layer 2: (k₂,L₂).
- Boundary temperatures Tₕ > Tc.
At steady state, the same Q dot passes through each layer.
Physical interpretation:
- A multilayer wall behaves like resistors in series: the same heat current must pass through every layer, and each layer “uses up” a temperature drop proportional to its resistance.
- The layer with the largest Rᵢ = Lᵢ/(kᵢA) is the bottleneck and gets most of the temperature drop.
Bridge note:
- O-Level intuition says “heat goes through both layers.”
- UY1 upgrade treats each layer as a resistance and enforces equal heat current.
Core derivation / explanation
For each layer,
Total temperature drop:
Hence
Interface temperature Tᵢ follows from either layer drop.
For cylindrical insulation (inner radius a, outer radius b, length L):
Equivalent radial thermal resistance:
Units check:
Physical sanity check:
- Adding insulation (larger Rₜₕ) decreases Q dot.
- In cylindrical form, increasing b increases ln(b/a) and reduces heat leak.
- Temperature drops are not “shared equally” unless the resistances are equal: Δ Tᵢ = Q dot Rᵢ. - The simple series result assumes the same area for all layers. If area changes (e.g. radial conduction), use the correct geometry-specific resistance. - For cylinders, the resistance is logarithmic in radius ratio ln(b/a), not proportional to thickness b-a. - Real walls can have contact resistances at interfaces; those add in series too.
Worked example
Heat flow through a two-layer wall
Worked example 1
Heat flow through a two-layer wall
Problem
A wall has area A = 1.0 m². Layer 1 has thickness 0.10 m and conductivity 0.80 W m⁻¹K⁻¹; layer 2 has thickness 0.05 m and conductivity 0.04 W m⁻¹K⁻¹. The outer faces are held at 30°C and 0°C. Assuming steady one-dimensional conduction, constant conductivities and negligible contact resistance, find the heat-flow rate and identify which layer has the larger temperature drop.
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Calculate each layer's resistance
Method
Replace each slab with its thermal resistance.Reason
The layers carry the same heat-flow rate, so their resistances add in series.Working
Answer
R₁ = 0.10/0.80(1.0) = 0.125 K W⁻¹, R₂ = 0.05/0.04(1.0) = 1.25 K W⁻¹.Apply the total temperature drop
Method
Divide the face-to-face temperature difference by the total resistance.Reason
A Celsius temperature difference has the same numerical value in kelvin, and the full 30 K drop spans both layers.Working
Answer
Q dot = 30/(0.125 + 1.25) = 21.8 W.Interpret the bottleneck
Working
Answer
The heat-flow rate is 21.8 W. Since Δ Tᵢ = Q dot Rᵢ, layer 2 has ten times the temperature drop of layer 1: about 27.3 K compared with 2.73 K. The thin insulating layer dominates the resistance.
Practice set
Check your understanding 1
Two equal-thickness slabs with constant conductivities form a wall. With the same face temperatures, area and ideal contact, does reversing their order reduce steady one-dimensional heat loss?
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Check your understanding 2
A wall has total resistance 1.375 K W⁻¹ and a fixed 30 K face-to-face temperature difference. A third layer adds 0.50 K W⁻¹ in series. Find the new heat-flow rate.
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Check your understanding 3
Why must the heat-flow rate entering an interface equal the rate leaving it at steady state?
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Summary + next steps
- Compound conduction is best solved with thermal-resistance networks.
- Same heat rate through all series layers is the central steady-state condition.
- Cylindrical geometry introduces logarithmic resistance.
Next steps:
- Compare with boundary-layer transport in UY1: convection.
- Then use combined convection-conduction resistances in UY1: convective heat transfer.
- Revisit the single-layer building block in UY1: conduction and compare radiative exchange in UY1: radiation.
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Syllabus and review details
No official syllabus alignment is listed for this lesson.