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For two diffuse gray surfaces in a two-surface enclosure, net heat transfer follows the fourth-power temperature difference and a resistance network.
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Formula
Q̇ in W; σ in W/(m2·K4); area in m2; temperature in K; ε and F dimensionless
| Symbol | Meaning | Unit |
|---|---|---|
| Q̇12 | Net radiation heat rate from surface 1 to 2 | W |
| Stefan–Boltzmann constant | W/(m2·K4) | |
| Absolute surface temperatures | K | |
| Hemispherical emissivities | dimensionless | |
| Exchange areas | m2 | |
| View factor from surface 1 to 2 | dimensionless |
\dot Q_{12}=\frac{\sigma(T_1^4-T_2^4)}{\frac{1-\varepsilon_1}{A_1\varepsilon_1}+\frac{1}{A_1F_{12}}+\frac{1-\varepsilon_2}{A_2\varepsilon_2}}This resistance relation assumes diffuse gray surfaces with constant emissivity exchanging radiation in a two-surface enclosure; other radiative paths must be excluded or modeled as additional network branches. Temperatures are absolute kelvin. View factors are geometric and obey reciprocity A1F12=A2F21. Convection, contact conduction, spectral behavior and nongray surfaces are not included.
This resistance relation assumes diffuse gray surfaces with constant emissivity exchanging radiation in a two-surface enclosure; other radiative paths must be excluded or modeled as additional network branches. Temperatures are absolute kelvin. View factors are geometric and obey reciprocity A1F12=A2F21. Convection, contact conduction, spectral behavior and nongray surfaces are not included.
For two diffuse gray surfaces in a two-surface enclosure, net heat transfer follows the fourth-power temperature difference and a resistance network.
Base equation for the target quantity
Preserve signs, boundary conditions and units when rearranging.
Work through the numerical example for “Net radiative heat transfer between gray surfaces” and check its unit and magnitude.
Let A1=1 m2, A2=2 m2, ε1=0.8, ε2=0.6, F12=0.5, T1=500 K and T2=300 K.
The denominator is 0.25+2+0.3333=2.5833 m−2; the numerator is about 3084.5 W/m2, giving Q̇12≈1194 W from 1 to 2.
The resistance has units m−2.
Substituting a related quantity that shares the same symbol.
Use variable definitions and check: Q̇ in W; σ in W/(m2·K4); area in m2; temperature in K; ε and F dimensionless.
Formula cluster
For two diffuse gray surfaces in a two-surface enclosure, net heat transfer follows the fourth-power temperature difference and a resistance network.
Let A1=1 m2, A2=2 m2, ε1=0.8, ε2=0.6, F12=0.5, T1=500 K and T2=300 K. The denominator is 0.25+2+0.3333=2.5833 m−2; the numerator is about 3084.5 W/m2, giving Q̇12≈1194 W from 1 to 2. The resistance has units m−2.
Estimate radiation exchange between furnace surfaces, shields and enclosures.
Here is how to work through a typical Net radiative heat transfer between gray surfaces (Radiation network with view factor F₁₂) task step by step:
Task
Work through the numerical example for “Net radiative heat transfer between gray surfaces” and check its unit and magnitude.
Solution path
Let A1=1 m2, A2=2 m2, ε1=0.8, ε2=0.6, F12=0.5, T1=500 K and T2=300 K.
The denominator is 0.25+2+0.3333=2.5833 m−2; the numerator is about 3084.5 W/m2, giving Q̇12≈1194 W from 1 to 2.
The resistance has units m−2.
Each diffuse gray surface emits ideally in proportion to σT4. Net exchange is therefore driven by σ(T14−T24), not a linear temperature difference. Near a reference temperature, it can be linearized approximately, but only locally. Always use kelvin because radiation depends on absolute temperature. Assumes diffuse gray surfaces in a two-surface enclosure. Use kelvin and geometrically reciprocal view factors. Application: Estimate radiation exchange between furnace surfaces, shields and enclosures. The numerical example Let A1=1 m2, A2=2 m2, ε1=0.8, ε2=0.6, F12=0.5, T1=500 K and T2=300 K. The denominator is 0.25+2+0.3333=2.5833 m−2; the numerator is about 3084.5 W/m2, giving Q̇12≈1194 W from 1 to 2. The resistance has units m−2 anchors the idea in a concrete measurement case.
F12 is the fraction of diffuse radiation leaving surface 1 that directly reaches surface 2. It depends on geometry and orientation, lies from zero to one and obeys reciprocity A1F12=A2F21. Shields or third surfaces change exchange paths, so one F12 term is then insufficient. Assumes diffuse gray surfaces in a two-surface enclosure. Use kelvin and geometrically reciprocal view factors. The corresponding units are Q̇ in W; σ in W/(m2·K4); area in m2; temperature in K; ε and F dimensionless. Let A1=1 m2, A2=2 m2, ε1=0.8, ε2=0.6, F12=0.5, T1=500 K and T2=300 K. The denominator is 0.25+2+0.3333=2.5833 m−2; the numerator is about 3084.5 W/m2, giving Q̇12≈1194 W from 1 to 2. The resistance has units m−2. This checks that the reference quantities are compatible.
The radiation network contains a surface resistance for the nonblack behavior of surface 1, a geometric space resistance from the view factor and a second surface resistance for surface 2. They act in series for this ideal exchange. Emissivity near one reduces surface resistance; poor view increases space resistance. All terms must refer to consistent areas. Assumes diffuse gray surfaces in a two-surface enclosure. Use kelvin and geometrically reciprocal view factors. Scope: This resistance relation assumes diffuse gray surfaces with constant emissivity exchanging radiation in a two-surface enclosure; other radiative paths must be excluded or modeled as additional network branches. Temperatures are absolute kelvin. View factors are geometric and obey reciprocity A1F12=A2F21. Convection, contact conduction, spectral behavior and nongray surfaces are not included. A practical application is Estimate radiation exchange between furnace surfaces, shields and enclosures.
If T1>T2, then T14−T24 is positive and heat flows from 1 to 2 under this sign convention. Swapping temperatures reverses the sign. The magnitude is net transfer, not gross radiation in both directions. Convection and conduction can add parallel heat paths and must be included separately in a total balance. Assumes diffuse gray surfaces in a two-surface enclosure. Use kelvin and geometrically reciprocal view factors. Check the calculation with this case: Let A1=1 m2, A2=2 m2, ε1=0.8, ε2=0.6, F12=0.5, T1=500 K and T2=300 K. The denominator is 0.25+2+0.3333=2.5833 m−2; the numerator is about 3084.5 W/m2, giving Q̇12≈1194 W from 1 to 2. The resistance has units m−2. Keep the model limits and units in view.
The example denominator is about 2.583 m−2 and σ(5004−3004) about 3084.5 W/m2. Dividing gives roughly 1194 W. The denominator has units m−2, so the numerator W/m2 yields watts. Heat flows from the hotter first surface to the cooler second surface. Assumes diffuse gray surfaces in a two-surface enclosure. Use kelvin and geometrically reciprocal view factors. The relation describes For two diffuse gray surfaces in a two-surface enclosure, net heat transfer follows the fourth-power temperature difference and a resistance network. This helps distinguish its target quantity from neighbouring quantities.
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