Skip to main content

Conduction through hollow sphere

Short answer

Spherical heat flow: Q = 4πk (T1−T2) / (1/r1 − 1/r2). With r1=0.1 m, r2=0.2 m, k=15 W/m·K, ΔT=200 K: Q = 4π·15·200 / (1/0.1−1/0.2) = 7.54 kW. At r=0.15 m, T = 300 − (7540/(4π·15))(1/0.1−1/0.15) = 166.7 °C.

A hollow sphere of inner radius 100 mm and outer radius 200 mm is made of material of thermal conductivity 15 W/m K. The inner surface is kept at 300 °C and the outer surface at 100 °C. Derive the expression you use for the heat flow, and calculate (a) the heat flow rate and (b) the temperature at a radius of 150 mm.

Expression for a hollow sphere

Steady radial conduction with no generation: ddr(r2dTdr)=0\dfrac{d}{dr}\left(r^2\dfrac{dT}{dr}\right)=0, so T=−C1/r+C2T = -C_1/r + C_2. Using Q=−k(4πr2)dTdrQ = -k(4\pi r^2)\dfrac{dT}{dr} and the boundary temperatures T1T_1 at r1r_1 and T2T_2 at r2r_2:

Q=4πk (T1−T2)1r1−1r2Q = \frac{4\pi k\,(T_1 - T_2)}{\dfrac{1}{r_1}-\dfrac{1}{r_2}}

and the temperature at any radius:

T=T1−Q4πk(1r1−1r)T = T_1 - \frac{Q}{4\pi k}\left(\frac{1}{r_1}-\frac{1}{r}\right)

(a) Heat flow

Given r1=0.1r_1 = 0.1 m, r2=0.2r_2 = 0.2 m, k=15k = 15 W/m K.

1r1−1r2=10−5=5 m−1Q=4π(15)(300−100)5=7540 W\begin{aligned} \frac{1}{r_1}-\frac{1}{r_2} &= 10 - 5 = 5\ \text{m}^{-1}\\ Q &= \frac{4\pi(15)(300-100)}{5} = 7540\ \text{W} \end{aligned}

(b) Temperature at 150 mm

T=300−75404π(15)(10−10.15)=300−40 (10−6.667)=300−133.3=166.7 ∘C\begin{aligned} T &= 300 - \frac{7540}{4\pi(15)}\left(10 - \frac{1}{0.15}\right)\\ &= 300 - 40\,(10 - 6.667) = 300 - 133.3 = 166.7\ ^\circ\text{C} \end{aligned}

The temperature at r = 0.15 m (166.7 °C) is lower than the arithmetic mean of the surfaces (200 °C), because the area is smaller near the inside and the gradient is steeper there.

Answer: Q≈7.54 kWQ \approx 7.54\ \text{kW}; T(0.15 m)≈166.7 ∘CT(0.15\ \text{m}) \approx 166.7\ ^\circ\text{C}.

✓ Answer checked by Claude Sonnet 5.5

All Heat Transfer chapter 2 questions →