Nusselt Number Calculator

The Nusselt number calculator helps you determine the relation between convective heat and conduction heat transfer between a fluid and a surface. This article will cover the Nusselt number equation, the acceptable range for the Nusselt number in natural convection, and when fluid flows through a pipe. Thus, if you have ever wondered how much convection can enhance heat transfer, this article is for you.

The Nusselt number is a dimensionless number that engineers use to describe the heat transfer rate between a fluid and a solid surface. It indicates how much heat transfer occurs due to convection compared to conduction.

Because of its meaning, engineers use the Nusselt number when designing equipment where heat transfer is the main objective, such as boilers or machinery cooling pipes.

Because of the primary definition of the Nusselt number, its equation is as follows:

where:

• $\rm Nu$ – Nussel number, dimensionless;
• $q_{\rm conv}$ – Heat transfer due to convection; and
• $q_{\rm cond}$ – Heat transfer due to conduction.

A higher Nusselt number indicates efficient convective heat transfer, which will increase the overall heat transfer coefficient, as we explain in the heat transfer coefficient calculator.

We can write the Nusselt number formula explained above as a relation of convective heat transfer coefficient, characteristic length, and fluid thermal conductivity:

where:

• $h_{c}$ – Convective heat transfer coefficient, expressed in $\footnotesize \rm{ W/m^2⋅K}$.
• $L$ – Characteristic length of the solid surface, expressed in $\footnotesize \rm{m}$. Remember that the characteristic length is typically the solid surface's length in the heat transfer direction.
• $k_{f}$ – Thermal conductivity of the fluid, expressed in $\footnotesize \rm{ W/m⋅K}$.

The above formula applies in all situations, but what if we cannot calculate the convective heat transfer coefficient? In that situation, we must use empirical correlations that involve other heat transfer dimensionless numbers such as the Reynolds number, Rayleigh number, and Prandtl number. Different combinations between them help you calculate the Nusselt number for natural convection and forced flow convection.

For natural convection, the Nusselt number range is over 1 and below 10, and the Rayleigh number determines it.

For vertical plates and cylinders like pipes, we have the following equation:

where:

• $\rm Ra$ – Rayleigh number; and,
• $C$, and $n$ – Nusselt number coefficients for natural convection.

We are going to cover laminar and turbulent scenarios for vertical plates and isothermic cylinders:

Because we have flow velocity, we change the strategy and start using not only the Reynolds number but also the Prandtl number:

where:

• $\rm Re$ – Reynolds number; and
• $\rm Pr$ – Prandtl number – both dimensionless.

We are going to cover laminar and turbulent scenarios for flat plates and isothermic cylinders/pipes:

Do not worry if you think we have so many formulas. Our excellent Nusselt number calculator includes them all in Advanced calculator options.

Let's assume you want to preserve the temperature of a natural gas pipe, and you will use a water heat exchanger. Consider the gas going through a pipe and getting heated with an isothermic external temperature. To obtain the Nusselt number of the fluid, we do the following:

1. Recognize it is a forced fluid/inside of a pipe/heating situation; thus, the Nusselt number equation we are going to use is $\rm \footnotesize 0.023 \times Re^{0.8} \times Pr^{0.4}$.

2. Assuming $\rm\footnotesize Re = 10.1^4$ and $\rm\footnotesize Pr = 1$, we obtain a Nusselt number of 37.64.

Therefore, the heating made by external water to the gas inside the pipe improves the heat transfer, and the heat transferred through convection is 37.6 times compared to the conductive heat transfer. This is a proper result of highly turbulent flow, which is true because we have a Reynolds number above 3500.