The fins attached to a surface are determined to have an effectiveness of \(0.9\). Do you think the rate of heat transfer from the surface has increased or decreased as a result of the addition of these fins?

Short Answer

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Answer: The rate of heat transfer from the surface has decreased due to the addition of fins with an effectiveness of 0.9.

Step by step solution

01

Define effectiveness

Effectiveness (\(\epsilon\)) is a dimensionless quantity that compares the heat transfer rate between a finned surface and an unfinned surface. An effectiveness value of 1 means the heat transfer rate is the same with or without the fins, while a value greater than 1 indicates improved heat transfer. If the effectiveness is less than 1, the fins reduce heat transfer.
02

Compare the given effectiveness value with 1

In this exercise, the effectiveness of the fins attached to the surface is given as \(\epsilon = 0.9\). Our task is to determine whether this value indicates an increase or decrease in the rate of heat transfer.
03

Determine the effect of fins on heat transfer rate

Since the effectiveness value is \(\epsilon = 0.9\), which is less than 1, we can conclude that the rate of heat transfer from the surface has decreased due to the addition of these fins.

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Key Concepts

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

Heat Transfer Enhancement
Understanding heat transfer enhancement is crucial for developing more efficient thermal systems. In thermal engineering, fins are widely used to increase the surface area available for heat transfer, thus potentially improving the overall heat dissipation from a surface.

Consider a finned surface, for which the term 'effectiveness' quantifies the improvement in heat transfer when compared to an unfinned surface. The higher the effectiveness, the more pronounced the heat transfer enhancement. However, in our exercise, the effectiveness is given as 0.9, meaning that instead of enhancing, it implies a decrease in heat transfer, which might seem counterintuitive. This situation could arise due to various practical factors such as additional thermal resistance introduced by the fins or poor fin design.

To really enhance heat transfer, fins must be designed to provide a net positive effect. This requires careful consideration of material, geometry, and placement so that the added conduction and convection processes facilitated by the fins outweigh any potential disadvantages.
Thermal Engineering Education
In thermal engineering education, it's essential to convey the real-world complexities of heat transfer processes to students. Through solving textbook exercises, such as the one concerning fin effectiveness, students gain insight into the subtleties of thermal systems and learn how to apply theoretical concepts in practical scenarios.

Educators should emphasize that not all thermal solutions, such as the addition of fins, will automatically enhance heat transfer. The analysis of fin effectiveness, involving a comparison of actual performance against the ideal scenario, is a key learning outcome. Students should also be made aware of the importance of conducting experiments and simulations in conjunction with theoretical studies to fully grasp the performance of thermal systems.
Dimensionless Quantities in Heat Transfer
Dimensionless quantities play a vital role in the analysis of heat transfer problems. They allow engineers and students to draw comparisons between different thermal systems without the need for specific unit measurements. Effectiveness, as highlighted in the exercise, is one such quantity.

Effectiveness highlights the ratio of the actual heat transfer to the maximum possible heat transfer. It is deeply tied to other dimensionless numbers, such as the Nusselt number, which relates the convective to the conductive heat transfer at a surface, or the Biot number, which compares the internal resistance within a body to the external resistance to heat transfer.

By understanding these quantities, students can better grasp the principles of scale similarity and nondimensional analysis, which are indispensable in thermal engineering for designing experiments, comparing thermal systems, and developing new heat transfer solutions.

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Most popular questions from this chapter

Chilled water enters a thin-shelled 5-cm-diameter, 150-mlong pipe at \(7^{\circ} \mathrm{C}\) at a rate of \(0.98 \mathrm{~kg} / \mathrm{s}\) and leaves at \(8^{\circ} \mathrm{C}\). The pipe is exposed to ambient air at \(30^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(9 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). If the pipe is to be insulated with glass wool insulation \((k=0.05 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) in order to decrease the temperature rise of water to \(0.25^{\circ} \mathrm{C}\), determine the required thickness of the insulation.

Exposure to high concentration of gaseous ammonia can cause lung damage. To prevent gaseous ammonia from leaking out, ammonia is transported in its liquid state through a pipe \(\left(k=25 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, D_{i}=2.5 \mathrm{~cm}\right.\), \(D_{o}=4 \mathrm{~cm}\), and \(L=10 \mathrm{~m}\) ). Since liquid ammonia has a normal boiling point of \(-33.3^{\circ} \mathrm{C}\), the pipe needs to be properly insulated to prevent the surrounding heat from causing the ammonia to boil. The pipe is situated in a laboratory, where the average ambient air temperature is \(20^{\circ} \mathrm{C}\). The convection heat transfer coefficients of the liquid hydrogen and the ambient air are \(100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and \(20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), respectively. Determine the insulation thickness for the pipe using a material with \(k=\) \(0.75 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) to keep the liquid ammonia flowing at an average temperature of \(-35^{\circ} \mathrm{C}\), while maintaining the insulated pipe outer surface temperature at \(10^{\circ} \mathrm{C}\).

Computer memory chips are mounted on a finned metallic mount to protect them from overheating. A \(152 \mathrm{MB}\) memory chip dissipates \(5 \mathrm{~W}\) of heat to air at \(25^{\circ} \mathrm{C}\). If the temperature of this chip is to not exceed \(50^{\circ} \mathrm{C}\), the overall heat transfer coefficient- area product of the finned metal mount must be at least (a) \(0.2 \mathrm{~W} /{ }^{\circ} \mathrm{C}\) (b) \(0.3 \mathrm{~W} /{ }^{\circ} \mathrm{C}\) (c) \(0.4 \mathrm{~W} /{ }^{\circ} \mathrm{C}\) (d) \(0.5 \mathrm{~W} /{ }^{\circ} \mathrm{C}\) (e) \(0.6 \mathrm{~W} /{ }^{\circ} \mathrm{C}\)

Superheated steam at an average temperature \(200^{\circ} \mathrm{C}\) is transported through a steel pipe \(\left(k=50 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, D_{o}=8.0 \mathrm{~cm}\right.\), \(D_{i}=6.0 \mathrm{~cm}\), and \(L=20.0 \mathrm{~m}\) ). The pipe is insulated with a 4-cm thick layer of gypsum plaster \((k=0.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\). The insulated pipe is placed horizontally inside a warehouse where the average air temperature is \(10^{\circ} \mathrm{C}\). The steam and the air heat transfer coefficients are estimated to be 800 and \(200 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), respectively. Calculate \((a)\) the daily rate of heat transfer from the superheated steam, and \((b)\) the temperature on the outside surface of the gypsum plaster insulation.

A plane brick wall \((k=0.7 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) is \(10 \mathrm{~cm}\) thick. The thermal resistance of this wall per unit of wall area is (a) \(0.143 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\) (b) \(0.250 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\) (c) \(0.327 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\) (d) \(0.448 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\) (e) \(0.524 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\)

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