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Heat transfer and thermal systems

Temperature under a constant imposed surface flux

Temperature at depth x and time t in a semi-infinite solid heated at a constant surface flux q″, with ξ = x/(2√(αt)).

Ref
HTS-19
Rev
v1
Field
Heat transfer and thermal systems
Result
T [K]

With a constant heat flux q″ into the surface of a semi-infinite solid, the temperature at depth x is T = Ti + (q″/k)[2√(αt/π) exp(−ξ²) − x erfc(ξ)], with ξ = x/(2√(αt)). At the surface it gives Ts = Ti + 2q″√(αt/π)/k, rising as √t. An insulated back face must be beyond the affected region.

Temperature at depth x and time t in a semi-infinite solid heated at a constant surface flux q″, with ξ = x/(2√(αt)). Constant properties; an insulated back face must lie beyond the affected region.

Calculator

Solve for
K
K
2501,000
W/m²
101e7
W/(m K)
0.1500
m²/s
1e-80.001
s
11,000,000
m
00.5
  • Surface temperature, Ti + 2q″√(αt/π)/k356.4 K
  • Temperature rise at depth x5.025 K
  • Thermal penetration length, √(αt)0.01 m

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 depth x (K) current value 305 K
tTime since heating beganKey driver
3005,840
q″Surface heat flux into the solid
3005,330
αThermal diffusivity
3001,990
TiInitial temperature
2551,010
kThermal conductivity
300401
xDepth below the surface
300356
  • At 0.02 m deep the solid has warmed by 5.025 K, to 305 K, after 100 s.
  • The surface itself would be at 356.4 K, which is the temperature a surface sensor would read.
Chart data as tables

Ranked variables

VariableTypical rangeLowest resultHighest resultSwing (K)Local stepChange in result
t Time since heating began1 to 1,000,000 s3005,8425,542+10%+0.348 %
q″ Surface heat flux into the solid10 to 1e7 W/m²3005,3255,025+10%+0.165 %
α Thermal diffusivity1e-8 to 0.001 m²/s3001,9861,686+10%+0.348 %
Ti Initial temperature250 to 1,000 K2551,005750+10%+9.84 %
k Thermal conductivity0.1 to 500 W/(m K)300400.5100.5+10%−0.15 %
x Depth below the surface0 to 0.5 m300356.456.42+10%−0.452 %

Sweep of Depth below the surface

Depth below the surface (m)Temperature at depth x (K)
0356.4
0.0625300
0.125300
0.1875300
0.25300
0.3125300
0.375300
0.4375300
0.5300

Sweep one variable

Temperature at depth x (K)Hover, touch, or use the arrow keys on the chart
300310320330340350360 00.10.20.30.40.5 Depth below the surface (m) now 305

Variables and how each one contributes

T

Temperature at depth x

Result · K

What the equation gives you. Everything else feeds it.

Ti

Initial temperature

K · typical 250 to 1,000

The initial temperature, in K. Raises the temperature everywhere by the same amount. Raising it by 10 % (to 330) moves the result by +9.84 %, from 305 to 335 K.

q″

Surface heat flux into the solid

W/m² · typical 10 to 1e7

The constant surface heat flux into the solid, in W/m². Raises the temperature rise in direct proportion. Raising it by 10 % (to 11,000) moves the result by +0.165 %, from 305 to 305.5 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 2.2) moves the result by −0.15 %, from 305 to 304.6 K.

α

Thermal diffusivity

m²/s · typical 1e-8 to 0.001

The thermal diffusivity, in m²/s. A higher diffusivity spreads the heat deeper, lowering the surface rise but raising the deeper temperature. Raising it by 10 % (to 1.1×10−6) moves the result by +0.348 %, from 305 to 306.1 K.

t

Time since heating began

s · typical 1 to 1,000,000

The time since heating began, in s. More time raises the temperature, with the surface rise growing as √t. Raising it by 10 % (to 110) moves the result by +0.348 %, from 305 to 306.1 K.

x

Depth below the surface

m · typical 0 to 0.5

The depth below the surface, in m. A deeper point is cooler, since the heat has not reached it as much. Raising it by 10 % (to 0.022) moves the result by −0.452 %, from 305 to 303.6 K.

Worked example with the values above

  1. Penetration term: ξ = x/(2√(αt)) = 0.02 / (2 × 0.01) = 1.
  2. Bracket: 2√(αt/π) exp(−ξ²) − x erfc(ξ) = 0.0041511 − 0.003146 = 0.0010051 m.
  3. T = 300 + (10,000/2) × 0.0010051 = 305.03 K.

Assumptions and limits

  • A semi-infinite solid with constant properties, so the back face is not felt over the time considered.
  • A one-dimensional geometry, an ideal step or constant flux at the surface and a uniform initial temperature.

Common mistakes

  • Using the step-temperature solution for a surface heated at constant flux.
  • Using the formula once the back face is affected.
  • Mixing up the surface flux sign: positive q″ heats the solid.

Statistics and uncertainty

Thermophysical properties of soils, concrete and foods vary by 10 % to 50 % with moisture and composition, so early-time results are only as good as the diffusivity and effusivity values.

Where it is used

  • Quenching, ground and wall heating, and contact burns.
  • Interpreting thin-film and heat-flux sensors.

Maths you need

  • Thermal diffusivity: α = k/(ρcp)
  • Complementary error function: erfc(x) = 1 − erf(x)
  • Thermal effusivity: e = √(kρcp)

Related formulas

Practise this formula