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Insulation thickness & heat loss

Enter the hot or cold face, the ambient, and the surface temperature you want to hold. The calculator returns the thickness needed, the next stock size, and what the remaining loss amounts to over a year.

How this works →

Your figures

Steam line, vessel wall or cold room — a negative value is fine.

60 °C is the usual personnel-protection limit on a hot surface.

Mineral wool 0.040–0.050, PUF 0.022, EPS 0.036, calcium silicate 0.060.

Total area to be insulated, for the loss and cost figures.

Result

Thickness

Insulation thickness

k × (130 K) ÷ (10 W/m²K × 15 K)

39 mm
Next stock thickness

Insulation is bought in these steps, in one or two layers

40 mm

Heat flow

Heat flux

Through the surface at 50 °C into 35 °C air

150 W/m²
Total loss

Over 100 m²

15 kW
Annual energy

8,000 hours a year

120,000 kWh
Bare surface loss

What it would lose with no insulation at all — the saving

145 kW

Questions

What surface temperature should I target?
Sixty degrees is the usual personnel-protection limit on a surface someone can touch. Where the aim is saving energy rather than protecting people, the economic thickness is normally greater than the one safety alone requires.
Does this work for cold rooms and chilled lines?
Yes — enter a hot face below ambient and it works the same way. But a cold face also needs a vapour barrier on the warm side. Without one, moisture condenses inside the insulation, ice forms, and the insulation stops working. The calculator warns you when the face is below ambient.
Where does the surface coefficient come from?
Combined convection and radiation from a clad surface to still air is taken at 10 W per square metre per kelvin, which is the figure the trade sizes with. It is not truly constant — it rises with temperature difference and sharply with wind — so an exposed outdoor line needs more than this suggests.
What about pipe curvature?
This calculates on a flat basis, which is accurate for large vessels and slightly conservative for small-bore pipe, where curvature increases the outer surface area and thus the loss. For small pipe at high temperature, use the supplier's cylindrical tables.