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Consider film condensation on a vertical plate. Will the heat flux be higher at the top or at the bottom of the plate? Why?

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01

Understanding Film Condensation

Film condensation occurs when a vapor cools and turns into a liquid, forming a thin film on a cold surface like a vertical plate. The heat is conducted through the liquid film to the cold surface. The heat flux depends on the film thickness and temperature difference between the film and the cold surface.
02

Effect of Gravity

Gravity plays a significant role in film condensation on a vertical plate. The liquid film flows downward due to gravitational force, causing the film to become thicker as it moves down the plate. This increase in thickness leads to a reduction in heat flux at the bottom of the plate as compared to the top.
03

Nusselt's Theory and Heat Flux

According to Nusselt's theory of film condensation, for laminar flow on a vertical plate, the film thickness (δ) is given by the equation: \[ \delta = \left( \frac{4 \nu_{L} x}{g \Delta T} \right)^{1/4} \] where: - \( \delta \) is the film thickness - \( \nu_{L} \) is the kinematic viscosity of the liquid - x is the distance from the top of the plate - g is the acceleration due to gravity - \( \Delta T \) is the temperature difference between the film and the cold surface Since the film thickness (δ) increases with x (distance from the top of the plate), the heat flux decreases as we move from the top to the bottom of the plate.
04

Conclusion

In conclusion, the heat flux will be higher at the top of the vertical plate compared to the bottom. This is because the liquid film becomes thicker as it moves downward due to gravity, and the thickness of the film plays a major role in determining the heat flux.

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Heat Flux
Heat flux is a term used to describe the rate of heat energy transfer through a surface. In the context of film condensation on a vertical plate, it is crucial to understand how this transfer occurs. The rate at which heat moves depends on several factors, such as the temperature difference across the film, the thermal conductivity of the material, and the thickness of the liquid film.

The thinner the film, the higher the heat flux, since a thinner film means heat can be conducted more efficiently to the cold surface. Now, imagine the process of condensation at the top of the plate. Here, the film starts thin, allowing a larger heat flux. As it travels down the plate, gravity causes the film to thicken, reducing the rate of heat transfer.
Vertical Plate
The vertical plate in our discussion serves as a surface for condensation. In heat transfer studies, vertical plates are often used to observe how fluids behave under the influence of gravity.

In film condensation scenarios, a vertical plate allows us to see how gravity affects the thickness of a liquid film. At the top of the plate, the film is at its thinnest. As the liquid film makes its way down, it gains thickness due to the accumulation of the liquid above it. This change in thickness is crucial for understanding how heat transfer rates alter from the top to the bottom of the plate.
Nusselt's Theory
Nusselt's theory provides us with a mathematical approach to understand film condensation over a surface. It helps in predicting the thickness of the film, assisting in determining the heat transfer efficiency. According to Nusselt's theory, the film thickness (\( \delta \)), in this case, increases with distance along the vertical plate due to gravitational forces.

The formula \[ \delta = \left( \frac{4 u_{L} x}{g \Delta T} \right)^{1/4} \]demonstrates that the film gets thicker as you move down the plate (where \( x \)is larger). Consequently, with greater film thickness, less heat flows through, impacting the overall heat flux.
Gravity Effect on Thermal Processes
Gravity is a silent yet powerful force influencing thermal processes like film condensation on a vertical plate. When a vapor condenses, it forms a liquid that is pulled downward by gravity. This creates a flow that increases the film thickness as it descends down the plate.

This thickness affects thermal conductivity, as a thicker film acts as an insulating layer, slowing down heat transfer. The interplay between gravity, plate orientation, and liquid properties defines how efficiently heat can be evacuated from the system. Understanding gravity's impact helps engineers optimize designs for better thermal management across various applications.

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Most popular questions from this chapter

Saturated steam at \(55^{\circ} \mathrm{C}\) is to be condensed at a rate of \(10 \mathrm{~kg} / \mathrm{h}\) on the outside of a \(3-\mathrm{cm}\)-outer-diameter vertical tube whose surface is maintained at \(45^{\circ} \mathrm{C}\) by the cooling water. Determine the required tube length. Assume wavylaminar flow, and that the tube diameter is large, relative to the thickness of the liquid film at the bottom of the tube. Are these good assumptions?

Saturated water vapor at atmospheric pressure condenses on the outer surface of a \(0.1\)-m-diameter vertical pipe. The pipe is \(1 \mathrm{~m}\) long and has a uniform surface temperature of \(80^{\circ} \mathrm{C}\). Determine the rate of condensation and the heat transfer rate by condensation. Discuss whether the pipe can be treated as a vertical plate. Assume wavy-laminar flow and that the tube diameter is large relative to the thickness of the liquid film at the bottom of the tube. Are these good assumptions?

Steam condenses at \(50^{\circ} \mathrm{C}\) on the outer surface of a horizontal tube with an outer diameter of \(6 \mathrm{~cm}\). The outer surface of the tube is maintained at \(30^{\circ} \mathrm{C}\). The condensation heat transfer coefficient is (a) \(5493 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (b) \(5921 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (c) \(6796 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (d) \(7040 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (e) \(7350 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (For water, use \(\rho_{l}=992.1 \mathrm{~kg} / \mathrm{m}^{3}, \mu_{l}=0.653 \times 10^{-3} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}\), \(\left.k_{l}=0.631 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, c_{p l}=4179 \mathrm{~J} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}, h_{f g} \oplus T_{\text {satl }}=2383 \mathrm{~kJ} / \mathrm{kg}\right)\) 10-130 Steam condenses at \(50^{\circ} \mathrm{C}\) on the tube bank consisting of 20 tubes arranged in a rectangular array of 4 tubes high and 5 tubes wide. Each tube has a diameter of \(6 \mathrm{~cm}\) and a length of \(3 \mathrm{~m}\), and the outer surfaces of the tubes are maintained at \(30^{\circ} \mathrm{C}\). The rate of condensation of steam is (a) \(0.054 \mathrm{~kg} / \mathrm{s}\) (b) \(0.076 \mathrm{~kg} / \mathrm{s}\) (c) \(0.315 \mathrm{~kg} / \mathrm{s}\) (d) \(0.284 \mathrm{~kg} / \mathrm{s}\) (e) \(0.446 \mathrm{~kg} / \mathrm{s}\) (For water, use \(\rho_{l}=992.1 \mathrm{~kg} / \mathrm{m}^{3}, \mu_{l}=0.653 \times 10^{-3} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}\), \(\left.k_{l}=0.631 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, c_{p l}=4179 \mathrm{~J} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}, h_{f g \otimes T_{\text {sat }}}=2383 \mathrm{~kJ} / \mathrm{kg}\right)\)

Saturated water vapor at a pressure of \(12.4 \mathrm{kPa}\) is condensed over an array of 100 horizontal tubes, each with a diameter of \(8 \mathrm{~mm}\) and a length of \(1 \mathrm{~m}\). The tube surfaces are maintained with a uniform temperature of \(30^{\circ} \mathrm{C}\). Determine the condensation rates of the tubes for \((a)\) a rectangular array of 5 tubes high and 20 tubes wide and \((b)\) a square array of 10 tubes high and 10 tubes wide. Compare and discuss the results of (a) and (b).

A 2-mm-diameter cylindrical metal rod with emissivity of \(0.5\) is submerged horizontally in water under atmospheric pressure. When electric current is passed through the metal rod, the surface temperature reaches \(500^{\circ} \mathrm{C}\). Determine the power dissipation per unit length of the metal rod.

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