Kitchen water at \(10^{\circ} \mathrm{C}\) flows over a 10 -cm-diameter pipe with a velocity of \(1.1 \mathrm{~m} / \mathrm{s}\). Geothermal water enters the pipe at \(90^{\circ} \mathrm{C}\) at a rate of \(1.25 \mathrm{~kg} / \mathrm{s}\). For calculation purposes, the surface temperature of the pipe may be assumed to be \(70^{\circ} \mathrm{C}\). If the geothermal water is to leave the pipe at \(50^{\circ} \mathrm{C}\), the required length of the pipe is (a) \(1.1 \mathrm{~m}\) (b) \(1.8 \mathrm{~m}\) (c) \(2.9 \mathrm{~m}\) (d) \(4.3 \mathrm{~m}\) (e) \(7.6 \mathrm{~m}\) (For both water streams, use \(k=0.631 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=4.32\), \(\left.\nu=0.658 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}, c_{p}=4179 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\)

The Reynolds number (Re) is a dimensionless quantity that helps predict flow patterns in different fluid flow situations. It is an essential parameter in fluid dynamics, correlating with the potential for turbulent or laminar flow. The higher the Reynolds number, the more likely it is that the flow will be turbulent, which can significantly affect heat transfer efficiency.

To calculate the Reynolds number, the formula used is: \[ Re = \frac{\rho \times V \times D}{\mu} \] or the more commonly used \[ Re = \frac{V \times D}{u} \] where

• \( \rho \) is the density of the fluid (not needed if using kinematic viscosity),
• \( V \) is the velocity of the flow,
• \( D \) is the characteristic length (typically diameter for pipes),
• \( \mu \) is the dynamic viscosity of the fluid, and
• \( u \) is the kinematic viscosity of the fluid.

In our exercise, the Reynolds number was calculated using the velocity of the water, the diameter of the pipe, and the kinematic viscosity provided. The result indicated a high Reynolds number, suggesting turbulent flow, which is important for efficient heat transfer.

The Nusselt number (Nu) is another dimensionless number in fluid dynamics and heat transfer calculations, representing the ratio of convective to conductive heat transfer across a boundary. A higher Nusselt number implies greater convective heat transfer, and it’s used to calculate the heat transfer coefficient.

The Nusselt number is often calculated when designing or analyzing heat exchangers, as it is related to the efficiency by which a fluid transfers heat to the surface. The formula for Nusselt number in terms of the heat transfer coefficient (\( h \)), the characteristic length (\( L \)), and thermal conductivity (\( k \)) of the fluid is: \[ Nu = \frac{h \times L}{k} \]
For pipes and similar situations, the Dittus-Boelter equation is a popular empirical correlation used to estimate the Nusselt number for turbulent flow based on the Reynolds number and the Prandtl number (\( Pr \)), which is a measure of a fluid's thermal diffusivity. In the exercise, we calculated Nu using this equation, indicating the degree of convection that can be expected in the geothermal water flow inside the pipe.

The heat transfer coefficient (\( h \)) represents the heat transferred per unit area per unit temperature difference. It's a crucial factor in designing thermal systems, as it denotes the efficiency with which heat is transferred from a fluid to a surface or between fluids in heat exchange scenarios. The formula for calculating this coefficient using the Nusselt number is:\[ h = \frac{Nu \times k}{D} \]

This coefficient is influenced by several factors, such as the type of fluid, flow velocity, surface material, and temperature difference. In the provided exercise, we used the Nusselt number and thermal conductivity to calculate the heat transfer coefficient for the geothermal water flowing inside the pipe. This calculation is fundamental to determining the size and efficiency of heat exchangers, as it directly affects the heat transfer rate.

The Dittus-Boelter equation is an empirical correlation that provides a method for calculating the Nusselt number, and therefore the heat transfer coefficient, for fluids in turbulent flow through pipes. This equation is convenient because it requires only a few fluid properties, simplifying the task of heat transfer analysis.
The equation is expressed as:\[ Nu=0.023 \times Re^{0.8} \times Pr^{0.4} \]
where

• \( Re \) is the Reynolds number,
• \( Pr \) is the Prandtl number, and
• \( Nu \) is the Nusselt number.

In scenarios like our exercise, the fluid properties and flow conditions enable the use of this equation to derive a value for Nusselt number. It’s typically applied to cases where the fluid temperature is near the surface temperature, and there is significant fluid movement. Judicious use of the Dittus-Boelter equation, as demonstrated in our step-by-step solution, can lead to accurate results in computing the required lengths of pipes in heat exchangers.