In finding the Nusselt number (a dimensionless number for determining heat transfer) for an hexagonal cylinder in cross flow, there are two correlations (which are to be used as the consequent terms in a Sugeno inference method):
$$
\begin{aligned}
& \mathrm{Nu}_1=0.16 \mathrm{Re}^{0.633} \operatorname{Pr}^{1 / 3} \quad 5000<\operatorname{Re}<19,650 \\
& \mathrm{Nu}_2=0.0385 \operatorname{Re}^{0.728} \operatorname{Pr}^{1 / 3} \operatorname{Re}>19,650
\end{aligned}
$$
Re is the Reynolds number and $\operatorname{Pr}$ is the Prandtl number.
The Nusselt number is a function of convective heat transfer $(h)$, diameter of the hexagonal cylinder $(D)$ over which cooling fluid travels, and the conductivity of the material $(K)$ :
$$
\mathrm{Nu}=\frac{h D}{K}
$$
Both Re and Pr can be fuzzy due to uncertainty in the variables in velocity. It would be convenient to find Nu (output) based on Re and Pr (inputs) without having to do all the calculations. More specifically, there is uncertainty in calculating the Reynolds number because velocity is not known exactly:
$$
\operatorname{Re}=\frac{\rho V D}{\mu}
$$
where $\rho$ is the density, $V$ is the velocity, $D$ is the characteristic length (or pipe diameter), and $\mu$ is the dynamic viscosity. And there is also uncertainty in the value for the Prandtl number due to its constituents
$$
\operatorname{Pr}=\frac{v}{\alpha}
$$
where $v$ is the kinematic viscosity and $\alpha$ is the specific gravity.
Calculation of Nu is very involved and the incorporation of a rule-base can be used to bypass these calculations; we have the following rules to govern this process:
If Re is high and Pr is low $\longrightarrow$ Then Nu is low
If Re is low and Pr is low $\longrightarrow$ Then Nu is low
If Re is high and Pr is high $\longrightarrow$ Then Nu is medium
If Re is low and Pr is high $\longrightarrow$ Then Nu is medium
For this problem, conduct a Mamdani and a Sugeno inference, based on the membership functions given in Figs P5.35a, $b$, and $c$, and use the following inputs:
$$
\begin{aligned}
\mathrm{Re} & =19.65 \times 10^3 \\
\operatorname{Pr} & =275
\end{aligned}
$$