Thermal Resistance Calculator
Calculate thermal resistance, heat flow, and temperature profiles through walls and composite structures.
Thermal Resistance Turns Heat Flow into a Circuit-Like Balance
Thermal resistance expresses how strongly a layer or interface opposes steady heat transfer, allowing many conduction and convection problems to be combined like resistors. For one-dimensional conduction through a plane layer, Rcond=L/(kA). For convection at a surface, Rconv=1/(hA). The steady heat-transfer rate is Q̇=ΔT/Rtotal when resistances are arranged in series.
Parallel heat-flow paths combine using reciprocal resistance, analogous to electrical circuits. Contact resistance, radiation, cylindrical geometry, and changing area can require additional or different resistance expressions.
| Symbol | Meaning | Why it appears / units |
|---|---|---|
| Rth | Thermal resistance | K/W. |
| L | Layer thickness | m. |
| k | Thermal conductivity | W/(m·K). |
| h | Convective coefficient | W/(m²·K). |
The largest resistance in a series path often controls most of the temperature drop. Insulation works by increasing thermal resistance, while high-conductivity materials reduce it.
The largest series thermal resistance should dominate the temperature drop. For steady one-dimensional heat flow, Q=ΔT/Rtotal; increasing any series resistance lowers Q. If adding insulation makes the predicted heat flow larger under the same boundary temperatures, the network has been assembled incorrectly.
Worked Examples
Common Mistakes
Parallel paths add conductances: 1/Rtotal=Σ1/Ri.
Both L/(kA) and 1/(hA) depend on the heat-transfer area.
Radial conduction through cylinders and spheres has logarithmic or reciprocal-radius resistance forms because area changes with radius.
Frequently Asked Questions
Formula Explorer connections
Interpretation: This formula tracks heat, temperature, work, entropy or transport in a thermodynamic system. Assumption: Use absolute temperature where required and consistent energy units. Constant properties, equilibrium, ideal gases or negligible losses may be assumed.