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Heat transfer and thermal systems

Radial temperature in a heat-generating sphere

Temperature in a solid sphere of radius R with uniform volumetric heating q‴ and a fixed surface temperature Ts.

Ref
HTS-08
Rev
v1
Field
Heat transfer and thermal systems
Result
T [K]

A solid sphere with uniform heating and a fixed surface temperature has the profile T(r) = Ts + q‴(R² − r²)/(6k), with a factor 6 where the slab has 2 and the cylinder 4. The centre has zero radial gradient. The surface flux is q‴R/3 and the total heat is q‴ times the volume of the sphere.

Temperature in a solid sphere of radius R with uniform volumetric heating q‴ and a fixed surface temperature Ts. Constant conductivity; the radial gradient is zero at the centre.

Calculator

Solve for
K
K
2501,000
W/m³
1,0001e9
m
0.010.3
m
00.01
W/(m K)
0.1500
  • Centre temperature, Ts + q‴R²/(6k)322.5 K
  • Total heat generated, q‴ × 4πR³/367.86 W
  • Heat flux at the surface, q‴R/36,000 W/m²

What drives the result

Each variable is moved across its typical range while the others stay at the values above. The longest bar is the key driver.

Temperature at r (K) current value 320 K
q‴Volumetric heat generationKey driver
30033,600
RSphere radius
3002,550
kThermal conductivity
3001,100
TsSurface temperature
2701,020
rRadius of interest
323
  • At r = 0.01 m the temperature is 320 K, and the centre reaches 322.5 K.
  • The sphere generates 67.86 W in total, so for the same R, k and q‴ a sphere runs cooler at its centre than a cylinder (factor 6 against 4).
Chart data as tables

Ranked variables

VariableTypical rangeLowest resultHighest resultSwing (K)Local stepChange in result
q‴ Volumetric heat generation1,000 to 1e9 W/m³30033,63033,330+10%+0.625 %
R Sphere radius0.01 to 0.3 m3002,5472,247+10%+1.48 %
k Thermal conductivity0.1 to 500 W/(m K)300.21,100799.8+10%−0.568 %
Ts Surface temperature250 to 1,000 K2701,020750+10%+9.38 %
r Radius of interest0 to 0.01 m320322.52.5+10%−0.164 %

Sweep of Radius of interest

Radius of interest (m)Temperature at r (K)
0322.5
0.00125322.5
0.0025322.3
0.00375322.1
0.005321.9
0.00625321.5
0.0075321.1
0.00875320.6
0.01320

Sweep one variable

Temperature at r (K)Hover, touch, or use the arrow keys on the chart
320321321322322323 00.0020.0040.0060.0080.01 Radius of interest (m) now 320

Variables and how each one contributes

T

Temperature at r

Result · K

What the equation gives you. Everything else feeds it.

Ts

Surface temperature

K · typical 250 to 1,000

The surface temperature, in K. Raises the temperature everywhere by the same amount. Raising it by 10 % (to 330) moves the result by +9.38 %, from 320 to 350 K.

q‴

Volumetric heat generation

W/m³ · typical 1,000 to 1e9

The uniform volumetric heat generation, in W/m³. Raises the temperature rise above the surface in direct proportion. Raising it by 10 % (to 660,000) moves the result by +0.625 %, from 320 to 322 K.

R

Sphere radius

m · typical 0.01 to 0.3

The sphere radius, in m. A larger radius raises the temperature rise with the square of R. Raising it by 10 % (to 0.033) moves the result by +1.48 %, from 320 to 324.7 K.

r

Radius of interest

m · typical 0 to 0.01

The radius at which the temperature is wanted, in m. Moving outwards lowers the temperature towards Ts. Raising it by 10 % (to 0.011) moves the result by −0.164 %, from 320 to 319.5 K.

k

Thermal conductivity

W/(m K) · typical 0.1 to 500

The thermal conductivity, in W/(m K). A higher conductivity lowers the temperature rise in inverse proportion. Raising it by 10 % (to 4.4) moves the result by −0.568 %, from 320 to 318.2 K.

Worked example with the values above

  1. Geometry term: R² − r² = 0.03² − 0.01² = 8×10−4 m².
  2. Rise above the surface: 600,000 × 8×10−4 / (6 × 4) = 20 K.
  3. T = 300 + 20 = 320 K.

Assumptions and limits

  • Uniform volumetric generation and constant conductivity in a steady state.
  • The stated boundary condition holds exactly, for example a fixed surface temperature or an insulated inner surface.

Common mistakes

  • Mixing the factor 2, 4 or 6 between the slab, cylinder and sphere.
  • Using the half-thickness or the full thickness in the wrong place.
  • Forgetting that generation is per unit volume, not per unit area.

Statistics and uncertainty

Volumetric heating is often known only to 10 % to 20 %, and the peak temperature scales directly with it. Use a margin on predicted centreline or hot-spot temperatures.

Where it is used

  • Hot-spot checks in busbars, fuel rods, heated plates and spherical particles.
  • Finding the surface temperature a coolant must hold for a given peak.

Maths you need

  • Volumetric generation: q‴ in W/m³
  • Steady conduction equation: k∇²T + q‴ = 0
  • Symmetry: zero gradient at the centre

Related formulas

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