Estimate convective losses for pipes and fins. Switch units instantly and explore design what‑ifs safely. Get clear outputs, heat flux, and engineering insights fast.
This tool applies Newton’s law of cooling for convection: Q = h · A · (Ts − T∞). Here, Q is heat transfer rate, h is the convection coefficient, A is exposed area, and (Ts − T∞) is the temperature difference.
| Case | h (W/m²·K) | A (m²) | Ts (°C) | T∞ (°C) | ΔT (K) | Q (W) |
|---|---|---|---|---|---|---|
| Natural convection (small surface) | 8 | 0.60 | 60 | 25 | 35 | 168 |
| Forced air flow (moderate) | 35 | 1.20 | 90 | 30 | 60 | 2520 |
| High convection (enhanced) | 120 | 0.75 | 120 | 35 | 85 | 7650 |
This tool applies Newton’s cooling relation, Q = hA(Ts − T∞), to estimate convective heat transfer. It converts inputs to SI, solves the selected variable, and reports heat flux q″ = hΔT. Use it for quick sizing and cross‑checks.
The coefficient h captures fluid properties, flow regime, geometry, and turbulence. Area A is the wetted surface exposed to the fluid. Ts is the boundary temperature; T∞ is the bulk fluid temperature.
Benchmarks help catch unit mistakes: natural convection in air is often 2–10 W/m²·K, forced air frequently 10–200 W/m²·K, and forced water may reach 500–10,000 W/m²·K. Values vary with speed and characteristic length.
ΔT = Ts − T∞ sets the direction. If Ts < T∞, ΔT is negative and Q is negative, meaning the surface gains heat from the fluid. For magnitude only, enable “magnitude mode” to report |ΔT|, |q″|, and |Q|.
For plates, A is the exposed face area. For cylinders, use lateral area A = πDL over the convecting length. For finned parts, include fin area plus exposed base. Since Q scales with A, geometry assumptions matter.
Start with an h range from correlations or vendor data, then compute Q at your expected Ts and T∞. Compare q″ against material or coating limits. Adjust flow (fan, pump), area (fins), or allowable temperatures to meet the target.
h is usually the largest uncertainty because small flow changes can shift it significantly. Other pitfalls include using inlet temperature instead of bulk temperature, ignoring radiation, and mixing units across inputs. Treat results as an estimate unless h is validated.
Convection drives performance in electronics cooling, heat exchangers, HVAC coils, and piping. When conduction through walls or radiation is comparable, combine terms in an overall balance. Exported reports support reviews and traceability.
h summarizes how efficiently the fluid exchanges heat with the surface. It depends on fluid properties, velocity, geometry, and turbulence, so it is commonly obtained from correlations, simulations, or experiments.
If Ts is below T∞, the surface is colder than the fluid. The sign indicates heat flows from the fluid to the surface. Enable magnitude mode if you only need the heat-transfer size.
Yes. Temperature differences have the same numerical value in kelvin and degrees Celsius. Differences in °F are larger by a factor of 9/5.
Use the lateral area A = πDL, where D is outer diameter and L is the length exposed to convection. Add end areas only if the ends are exposed and significant.
Natural convection in air is often 2–10 W/m²·K. Forced air commonly spans 10–200 W/m²·K depending on speed and turbulence. Use a correlation matched to your geometry for better accuracy.
No. This calculator focuses on convection. If radiation is relevant, compute radiative heat transfer separately and combine it with the convective term in an overall energy balance.
Yes. Choose Ts or T∞ in the “Solve for” menu, then enter Q, h, and A with the known temperature. The calculator rearranges Newton’s law and reports the solved temperature.
Important Note: All the Calculators listed in this site are for educational purpose only and we do not guarentee the accuracy of results. Please do consult with other sources as well.