Hot Water Heat Loss Calculator
Calculate heat loss from hot water pipes or storage tanks based on temperature difference, insulation, and geometry.
Steel ≈ 50, Copper ≈ 385, Plastic ≈ 0.4
Results will appear here.
Formulas Used
Pipe (Cylindrical Geometry) — Fourier's Law for radial conduction:
Q = ΔT / Rtotal
Rtotal = 1/(hi·2πr₁L) + ln(r₂/r₁)/(2πkwallL) + ln(r₃/r₂)/(2πkinsL) + 1/(ho·2πr₃L)
Where: r₁ = inner radius, r₂ = outer pipe radius, r₃ = outer insulation radius, L = pipe length
Tank (Flat-Wall / Planar Geometry):
Q = ΔT / Rtotal
Rtotal = 1/(hi·A) + twall/(kwall·A) + tins/(kins·A) + 1/(ho·A)
Auto surface area (spherical): A = 4π·(3V/4π)2/3
Tank temperature drop: ΔTdrop = Q·t / (m·cp), where m = mass of water, cp = 4186 J/(kg·K)
Total energy loss: E = Q × t (kWh)
Assumptions & References
- Water density assumed as 1 kg/L for temperature drop calculation.
- Specific heat of water: cp = 4186 J/(kg·K) (Incropera & DeWitt, Fundamentals of Heat and Mass Transfer).
- Tank wall thickness assumed 5 mm steel when using tank mode.
- Auto tank surface area calculated assuming a spherical shape (minimum surface area for a given volume).
- Pipe cylindrical resistance uses the standard logarithmic formula for radial conduction (ASHRAE Handbook — Fundamentals).
- Inner convective coefficient hi ≈ 300 W/m²·K is typical for turbulent water flow; ho ≈ 10 W/m²·K for natural convection in air.
- Insulation thermal conductivity: mineral wool ≈ 0.04 W/m·K, polyurethane foam ≈ 0.025 W/m·K (BS EN ISO 10211).
- Steady-state heat loss is assumed (temperature of water does not change significantly during the period — valid for short durations or well-heated systems).
- Reference: ISO 12241:2008 — Thermal insulation for building equipment and industrial installations.