Physics Lab

Heat Transfer — Conduction

In steady state, thermal energy flows from hot to cold through a material; Fourier's law quantifies the rate as proportional to area and temperature gradient.

Concept

Fourier's law (1-D steady state): dQdt=kAdTdx\frac{dQ}{dt} = -kA\frac{dT}{dx}

where kk is thermal conductivity (W/m·K). For a uniform slab of thickness LL: H=kA(T1T2)LH = \frac{kA(T_1 - T_2)}{L}

By analogy with electrical resistance, thermal resistance is Rth=L/(kA)R_{th} = L/(kA). Series resistances add; parallel conductances add.

Derivation

Two slabs in series, thicknesses L1,L2L_1, L_2 and conductivities k1,k2k_1, k_2. In steady state, the same heat current HH passes through both: H=k1A(T1Tm)L1=k2A(TmT2)L2H = \frac{k_1 A(T_1-T_m)}{L_1} = \frac{k_2 A(T_m-T_2)}{L_2}

Eliminating TmT_m: H=A(T1T2)L1/k1+L2/k2H = \frac{A(T_1-T_2)}{L_1/k_1 + L_2/k_2}

so the effective conductivity for equal-area slabs: L1+L2keff=L1k1+L2k2\frac{L_1+L_2}{k_{eff}} = \frac{L_1}{k_1} + \frac{L_2}{k_2}

For parallel slabs of equal length and different areas, the effective kk is area-weighted.

JEE Worked Example

Problem: A compound wall is made of two layers: 10 cm thick brick (k=0.8k=0.8 W/mK) and 5 cm thick wood (k=0.2k=0.2 W/mK). Outside is at 10-10°C, inside at 2525°C. Find the heat current per m² and the interface temperature.

Solution: Rbr=0.100.8=0.125,Rwd=0.050.2=0.25R_{br}=\frac{0.10}{0.8}=0.125,\quad R_{wd}=\frac{0.05}{0.2}=0.25 H/A=350.375=93.3  W/m2H/A = \frac{35}{0.375}=93.3\;\text{W/m}^2

Interface from inside: Tm=25HRwd=2593.3×0.25=1.7T_m = 25 - H R_{wd} = 25 - 93.3\times 0.25 = 1.7°C (wood between inside and brick).

Traps

  • Fourier's law assumes steady state; transient problems need the heat equation.
  • For radial conduction in a cylinder, H=2πkL(T1T2)/ln(r2/r1)H = 2\pi k L (T_1-T_2)/\ln(r_2/r_1) — not linear.
  • In series, the highest-resistance layer drops most of the temperature.
  • Don't confuse conductivity kk (intensive) with conductance kA/LkA/L (extensive).
  • For composite rods with different areas, area cancellation does not apply directly.

Key Takeaways

  • H=kAΔT/LH = kA\Delta T / L in 1-D steady state.
  • Rth=L/(kA)R_{th} = L/(kA); series adds, parallel like resistors.
  • The largest thermal-resistance layer controls heat flow.
  • Use radial form for cylindrical and spherical geometries.

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