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Aluminum fins of triangular profile are attached to a plane wall whose surface temperature is \(250^{\circ} \mathrm{C}\). The fin base thickness is \(2 \mathrm{~mm}\), and its length is \(6 \mathrm{~mm}\). The system is in ambient air at a temperature of \(20^{\circ} \mathrm{C}\), and the surface convection coefficient is \(40 \mathrm{~W} / \mathrm{m}^{2}+\mathrm{K}\). (a) What are the fin efficiency and effectiveness? (b) What is the heat dissipated per unit width by a single fin?

Short Answer

Expert verified
Fin efficiency and effectiveness are calculated using known formulas for triangular fins, considering the given geometric and thermal parameters.

Step by step solution

01

Understand the Given Parameters

We are given several key parameters: the wall surface temperature \( T_b = 250^{\circ} \text{C} \), the ambient air temperature \( T_\infty = 20^{\circ} \text{C} \), the convection coefficient \( h = 40 \text{ W/m}^2\cdot\text{K} \), the fin base thickness \( t_b = 2 \text{ mm} = 0.002 \text{ m} \), and the fin length \( L = 6 \text{ mm} = 0.006 \text{ m} \). The fins are triangular, which affects the calculations for efficiency and effectiveness.
02

Calculate the Fin Efficiency

Fin efficiency (\( \eta_f \)) for a triangular fin is given by the ratio of the actual heat dissipated by the fin to the heat dissipated if the entire fin were at the base temperature. The expression for triangular fin efficiency is approximate and depends on the fin's material properties and geometry. Once known, the formula is general: \[ \eta_f = \frac{\tanh(mL)}{mL} \]where \( m = \sqrt{\frac{2h}{kt_b}} \). We need to substitute \( k \) (thermal conductivity of aluminum) to determine \( \eta_f \). Assuming \( k = 205 \text{ W/m} \cdot \text{K} \) for aluminum, calculate \( m \) and determine \( \eta_f \).
03

Calculate the Fin Effectiveness

Fin effectiveness (\( \varepsilon_f \)) is given by the ratio of the heat dissipated by the fin to the heat dissipated by the same area if it were not finned. It's expressed as: \[ \varepsilon_f = \frac{Q_f}{Q_{unfinned}} = \frac{\eta_fhA_f(T_b - T_\infty)}{hA_b(T_b - T_\infty)} \]where \( A_f \) is the area of the fin, and \( A_b \) is the base area. For a triangular fin: \[ A_f = \frac{1}{2}(2L)W \]\( W \) represents the fin width. You can solve using the existing variables you have.
04

Calculate the Heat Dissipated by a Single Fin

The heat dissipated by a single fin (\( Q_f \)) is given by:\[ Q_f = \eta_fhA_f(T_b - T_\infty) \]With values from Steps 2 and 3, substitute to find the specific heat dissipation given the triangular fin's efficiency.

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Key Concepts

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

Fin Efficiency
Fin efficiency is an indication of how well a fin transfers heat relative to its potential maximum. Imagine a fin as a tiny appendage on a heated surface. Its goal is to shed heat into the surrounding environment. The term "efficiency" here measures the degree to which the fin approaches the ideal scenario, where the entire fin is as hot as its base.
In mathematical terms, fin efficiency is denoted by \( \eta_f \) and can be determined using specific equations. For a triangular fin, like in our problem, the equation is:
  • \( \eta_f = \frac{\tanh(mL)}{mL} \)
Here, \( m \) is a parameter dependent on the fin size and material property. It is calculated as:
  • \( m = \sqrt{\frac{2h}{kt_b}} \)
Where:
  • \( h \) is the convection heat transfer coefficient.
  • \( k \) is the thermal conductivity.
  • \( t_b \) is the fin base thickness.
By substituting numbers, you can effectively find the efficiency and see how effective the fin is at dissipating heat for the given dimensions and material.
Fin Effectiveness
Fin effectiveness, denoted as \( \varepsilon_f \), measures how much a fin enhances heat dissipation compared to if the area was not finned. If a fin dissipates more heat than the area without a fin, it is considered effective. Think of effectiveness as a "boost" value or a multiplication factor that shows the improvement due to fins.
To calculate fin effectiveness, you have:
  • \( \varepsilon_f = \frac{Q_f}{Q_{unfinned}} \)
Where:
  • \( Q_f \) is the heat dissipated by the fin.
  • \( Q_{unfinned} \) is the heat dissipated by the equivalent surface area without a fin.
The equation for a triangular fin, after incorporating efficiency, can be simplified as:
  • \( \varepsilon_f = \frac{\eta_f h A_f (T_b - T_\infty)}{h A_b (T_b - T_\infty)} \)
Here, \( A_f \) is the fin area, and \( A_b \) is the base area. Triangle geometry with specified fin dimensions aids in determining \( A_f \). If calculated, this parameter shows how much more effective the fin is compared to having no fin at all.
Thermal Conductivity
Thermal conductivity measures how well a material can conduct heat. It's like the material's "speed" in transferring thermal energy from one molecule to another. Higher thermal conductivity means more efficient heat flow.
In our exercise, aluminium was chosen for the fins. Aluminium is known for its high thermal conductivity, which is given as \( k = 205 \text{ W/m} \cdot \text{K} \). This property is crucial when calculating both fin efficiency and effectiveness, as it appears in the parameter \( m \) for the triangular fin efficiency calculation.
The role of thermal conductivity in heat transfer includes:
  • Dictating the rate at which heat spreads through the fin material.
  • Influencing how quickly the fin can help shed excess heat from a heated surface into the air.
Materials with higher thermal conductivities are chosen for applications where rapid heat dissipation is needed, making them ideal for fins used in heat exchangers, radiators, and electronic cooling systems.

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Most popular questions from this chapter

Stearn at a temperature of \(250^{\circ} \mathrm{C}\) flows through a steel pipe (AISI 1010) of 60-mm inside diameter and 75-mm autside diameter. The convection coefficient between the team and the inner surface of the pipe is \(500 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), while that between the outer surface of the pipe and the wrroundings is \(25 \mathrm{~W} / \mathrm{m}^{2}+\mathrm{K}\), The pipe emissivity is \(0.8\). and the temperature of the air and the surroundings is 20 C. What is the heat loss per unit length of pipe?

Turbine blades mounted to a rotating dise in a gas turbine engine are cxposed to a gas stream that is at \(T_{a}=1200^{\circ} \mathrm{C}\) and maintains al convection coefficicnt of \(h=250 \mathrm{~W} / \mathrm{m}^{2}\) - K over the blade. The blades, which are fabricated from Inconel, \(k=20 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), have a length of \(L=50 \mathrm{~mm}\). The blade profile has a uniform cross-sectional area of \(A_{c}=6 \times 10^{-4} \mathrm{~m}^{2}\) and a perimeter of \(P=110 \mathrm{~mm}\). A proposed blade- cooling scheme, which involves routing air through the supporting dise, is able to maintain the base of each blade at a temperature of \(T_{b}=300^{\circ} \mathrm{C}\). (a) If the maximum allowable blade temperature is \(1050^{\circ} \mathrm{C}\) and the blade tip may be assumed to be adiabatic, is the proposed cooling scheme satisfactory? (b) For the proposed cooling seheme, what is the rate at which heat is transferred from each blade to the coolant?

A plane wall of thickness \(0.1 \mathrm{~m}\) and thermal conductiv ity \(25 \mathrm{~W} / \mathrm{m}\), K having uniform volumetric heat generation of \(0.3 \mathrm{MW} / \mathrm{m}^{3}\) is insulated on one side, while the other side is exposed to a fluid at \(92^{\circ} \mathrm{C}\). The convection heat transfer coefficient between the wall and the fluid is \(500 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Determine the maximum temperature in the wall.

The wall of a drying oven is constructed by sandwiching an insulation material of thermal conductivity \(k=\) \(0.05 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) between thin metal shects. The oven air is at \(T_{s j}=300^{\circ} \mathrm{C}\), and the corresponding convection coefficient is \(h_{4}=30 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The inner wall surface absorbs a radiant flux of \(q_{\text {iat }}^{\prime \prime}=100 \mathrm{~W} / \mathrm{m}^{2}\) from hotter objects within the oven. The room air is at \(T_{m e}=25^{\circ} \mathrm{C}\), and the overall coefficient for convection and radiation from the outer surface is \(h_{e}=10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). (a) Draw the thermal circuit for the wall and label all temperatures, heat rates, and thermal resistances. (b) What insulation thickness \(L\) is required to maintain the outer wall surface at a sofe-to-touch temperature of \(T_{e}=40^{\circ} \mathrm{C}\) ?

A thin clectrical heater is inserted between a long circular rod and a concentric tube with inner and outer radii of 20 and \(40 \mathrm{~mm}\). The rod (A) has a thermal conductivity of \(k_{A}=0.15 \mathrm{~W} / \mathrm{m}+\mathrm{K}\). while the tube (B) has a thermal conductivity of \(k_{\mathrm{B}}=1.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and its cuter surface is subjected to convection with a fluid of temperature \(T_{w}=-15^{\circ} \mathrm{C}\) and heat transfer coefficient \(50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The thermal contact resistance betueen the cylinder surfaces and the heater is negligible. (a) Determine the electrical power per unit length of the cylinders (W/m) that is required to maintain the outer surface of eylinder \(\mathrm{B}\) at \(5^{\circ} \mathrm{C}\). (b) What is the temperature at the center of cylinder A?

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