Q = α·A·ΔT
Unlike conduction through a component, transfer between surface and fluid is captured directly via an empirical heat transfer coefficient, with no layer thickness involved.
Unlike conduction through a component, transfer between surface and fluid is captured directly via an empirical heat transfer coefficient, with no layer thickness involved.
Select a target and calculate.
Unlike conduction through a component, transfer between surface and fluid is captured directly via an empirical heat transfer coefficient, with no layer thickness involved.
α=25 W/(m²·K), A=2 m² and ΔT=8.4 K give Q=25·2·8.4=420 W.
Constant, area-averaged heat transfer coefficient α and steady state; the actual determination of α from flow regime, fluid and geometry (Nusselt correlations) is outside this calculator.
This calculator determines the heat flow between a surface and a flowing fluid, complementing existing conduction through solid components with convective transfer.
The Newtonian approach describes convective heat transfer as Q=α·A·ΔT, where α is an empirical heat transfer coefficient dependent on flow regime, fluid and geometry.
Q = α·A·ΔT
Q = α·A·ΔT| Symbol / input | Meaning |
|---|---|
| Heat flow Q | Heat flow transferred between surface and fluid. |
| Heat transfer coefficient α in W/(m²·K) | Empirical coefficient; free convection in air about 5 to 25, forced convection in air about 25 to 250, water considerably higher. |
| Transfer area A | Surface area involved in convection. |
| Temperature difference ΔT | Difference between surface temperature and fluid temperature outside the boundary layer. |
α is the heat transfer coefficient between surface and fluid, A the surface area involved, and ΔT the temperature difference between the surface and the fluid outside the boundary layer.
Take α from reference tables for the flow regime (free/forced, gas/liquid) and geometry involved, or compute it from a Nusselt correlation; take A and ΔT from the specific application.
α=25 W/(m²·K), A=2 m² and ΔT=8.4 K give Q=25·2·8.4=420 W.
A higher heat transfer coefficient (e.g. from forced convection or a fluid with high thermal conductivity) raises heat flow proportionally, all else equal.
A is an area, ΔT a temperature difference. Q is output as a power; α is entered as a dimensionless numerical value with the unit W/(m²·K) noted in the help text.
Estimating heat loss or gain at surfaces in an air or water flow, heat-sink sizing, and building-envelope calculations with a known α.
Constant, area-averaged heat transfer coefficient and steady state; the actual determination of α from flow regime, fluid properties and geometry via Nusselt, Reynolds and Prandtl numbers is outside this calculator.
Common mistake: Do not confuse α with the thermal conductivity λ of a solid; α describes transfer at the surface, λ conduction inside the component.
Estimating heat loss or gain at surfaces in an air or water flow, heat-sink sizing, and building-envelope calculations with a known α.
α is the heat transfer coefficient between surface and fluid, A the surface area involved, and ΔT the temperature difference between the surface and the fluid outside the boundary layer.
Constant, area-averaged heat transfer coefficient and steady state; the actual determination of α from flow regime, fluid properties and geometry via Nusselt, Reynolds and Prandtl numbers is outside this calculator.