1. Pipe and insulation
Model a uniform layer around a pipe held at a known outer-wall temperature.
2. Heat-transfer results
Enter inputs and calculate.
Positive heat transfer means heat loss from the pipe. Negative means heat gain into a cold pipe. The bare-pipe comparison uses the same wall temperature and external coefficient.
3. Compare insulation thicknesses
Same wall temperature, conductivity, and external coefficient for every row. These are comparison points, not product recommendations.
| Thickness (mm / in) | Heat (W/m) | Heat (Btu/h·ft) | Surface (°C / °F) | Magnitude reduction |
|---|
Calculation method
R′ins = ln(r₂/r₁) / (2πk)
R′surface = 1 / (2πr₂h)
q′ = (Tpipe − Tambient) / (R′ins + R′surface)
Tsurface = Tambient + q′ R′surface
Q = q′ L
Resistances per unit length are in m·K/W, q′ is W/m, and Q is W. At zero insulation thickness, the model reduces to the bare-pipe surface resistance.
Steady, one-dimensional radial conduction with uniform properties and full circumferential coverage. The entered pipe outer-wall temperature is fixed. Internal convection and pipe-wall resistance are not included. Neither are supports, valves, seams, wet insulation, solar heating, axial cooling, or end losses. Radiation is included only if you supply a suitable combined surface coefficient; the calculator does not calculate that coefficient.
The critical insulation radius is k/h for this constant-coefficient model. On sufficiently small pipes, adding a thin layer can increase heat transfer. A negative savings result is therefore possible. Surface temperature alone does not establish burn protection or condensation control.
Check the reported mean insulation temperature against your conductivity data. Actual conductivity and external heat transfer vary with temperature and installation conditions. For a planar stack, use Multi-Layer Heat Transfer.
