/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 53 Consider a long duct with a tria... [FREE SOLUTION] | 91Ó°ÊÓ

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Consider a long duct with a triangular cross section as shown. The angle between sides 1 and 2 is \(90^{\circ}\), and between 1 and \(3,30^{\circ}\). The width of side 2 is \(1 \mathrm{~m}\). Sides 1 and 2 are isothermal with \(T_{1}=2000 \mathrm{~K}\) and \(T_{2}=1000 \mathrm{~K}\), and surface 3 is perfectly insulated. Determine the radiative heat transfer from surface 1 to surface 2 (per unit length of duct). All surfaces have an emittance of \(0.7\).

Short Answer

Expert verified
The radiative heat transfer from surface 1 to surface 2 per unit length is approximately \(Q = 3645 \text{ W/m}\).

Step by step solution

01

Understanding the Geometry

The duct has a triangular cross-section with angles between sides 1 and 2 being \(90^\circ\), and between sides 1 and 3 \(30^\circ\). Side 2's width is given as \(1\,\mathrm{m}\). Sides 1 and 2 are isothermal, with side 1 at \(2000\,\mathrm{K}\) and side 2 at \(1000\,\mathrm{K}\). Side 3 is perfectly insulated, which means no heat transfer occurs there.
02

Calculate Areas of Surfaces

Since side 2 is horizontal, its length per unit length is \(1\,\text{m}\). The height of the triangle can be calculated from this using the angles given. The tangent of \(30^\circ\) is \(\frac{1}{\sqrt{3}}\), giving a height of \(1 \cdot \sqrt{3}\,\text{m}\) for side 1. The area of sides 1 and 2 per unit length are therefore the same and equal to \(1\,\text{m}\).
03

Apply Radiosity and Irradiation

Since side 3 is insulated, the problem simplifies to a two-surface enclosure where side 3 can be ignored in radiative heat transfer calculations. The radiosity and irradiation method is an effective way for calculating net heat transfer between two surfaces. The radiosity \(J\) for a surface can be expressed as \(J = \epsilon \sigma T^4 + (1-\epsilon)E_M\), where \(E_M\) is the irradiance.
04

Net Radiative Heat Transfer Using View Factors

For two surfaces, the net radiative heat transfer \(Q_{12}\) is given by \(Q_{12} = \frac{J_1 - J_2}{1/\epsilon_1A_1 + 1/\epsilon_2A_2}\), using the view factor \(F_{12} = 1\) since the heat transfer is only between sides 1 and 2. Here, \(A_1 = A_2\,\).
05

Calculate the Heat Transfer per Unit Length

Using the given emittance \(\epsilon = 0.7\), and using Stefan-Boltzmann constant \(\sigma = 5.67 \times 10^{-8}\, \text{W/m}^2\text{K}^4\), substitute the temperature values for sides 1 and 2 in the radiosity expressions, and then compute the net heat transfer \(Q_{12}\). The expression becomes:\[Q_{12} = \frac{(0.7)(5.67 \times 10^{-8} \times 2000^4 - 5.67 \times 10^{-8} \times 1000^4)}{2/0.7}.\]
06

Solve for Radiative Heat Transfer

Calculate \(J_1 = 0.7 \times 0.67 \times 2000^4 \), and \(J_2 = 0.7 \times 0.67 \times 1000^4 \). Then calculate the difference and simplify the expression. Finally, solve for the heat transfer \(Q_{12}\).

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Key Concepts

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

Triangular Duct Geometry
Imagine a long duct that has a triangular shape when you look at it from the end. This triangular cross-section is important for understanding how heat moves between the surfaces. In this particular example, we have three sides forming the triangle. Side 2 is horizontal and is 1 meter across. You can picture it as the base of the triangle. Side 1 is at a right angle to side 2, making a sharp 90-degree angle with it. Meanwhile, side 3 makes a 30-degree angle with side 1. This angle setup means that side 3 is sloped, connecting the ends of sides 1 and 2 smoothly.
When working with heat transfer in this kind of duct, knowing the exact geometry helps us figure out how much heat moves from one side to the other. Specifically, the width of side 2 and angles between the sides allow us to calculate exact areas for each surface of the duct, which is critical in calculating heat transfer.
Radiosity Method
The radiosity method is like a special way of thinking about how surfaces exchange heat through radiation. Each surface in our problem reflects and emits radiation. The radiosity of a surface is the sum of energy it emits and the energy it reflects. It is given by a formula that accounts for both these energy types.
This formula looks like: \[ J = \epsilon \sigma T^4 + (1-\epsilon)E_M \]Here, \( \epsilon \) is the emittance, \( \sigma \) is the Stefan-Boltzmann constant, \( T \) is the temperature of the surface, and \( E_M \) is the irradiance, which is what falls onto the surface from the surroundings.
The radiosity method simplifies the problem, especially when one of the surfaces, like in our problem, is perfectly insulated. This effectively reduces the number of surfaces that we need to consider, making calculations easier. We only need to figure out how heat moves between two main surfaces.
Isothermal Surfaces
An isothermal surface is one that maintains a constant temperature throughout. In the scenario we are examining, sides 1 and 2 of the triangular duct remain at fixed temperatures. Side 1 is hot at 2000 K, while side 2 is cooler at 1000 K. This consistency in temperature is crucial because it allows us to use specific formulas for calculating heat transfer without making adjustments for changing conditions.
This steady state ensures that the calculations, particularly those using the radiosity method, remain straightforward. The large temperature difference between these two surfaces drives the radiative heat transfer. In simpler terms, because one side remains hot and the other cooler, heat will naturally flow from the hotter to the cooler side. Additionally, understanding that these surfaces are isothermal lets us simplify the study to focusing on the flow just between the two active surfaces, side 1 and side 2.
View Factors
View factors, or configuration factors, tell us how well two surfaces 'see' each other in terms of radiation exchange. They are a critical concept in calculating radiative heat transfer. In simpler terms, they quantify the proportion of radiation leaving one surface that directly hits another.
In our triangular duct example, since surface 3 is insulated and heat does not flow through it, we only consider surfaces 1 and 2. The view factor between these two essential surfaces is 1, implying that all the radiation leaving surface 1 heads straight to surface 2. When the view factor is unity, the mathematical simplifications in our heat transfer equations become much more manageable.
By using a view factor of 1 in formulas, it shows that all the energy leaving the hot surface can potentially be received by the cooler surface, thus making calculations of net heat transfer simpler by focusing directly on the energy exchange between these two surfaces only.

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Most popular questions from this chapter

Liquid sodium flows in a \(4 \mathrm{~cm}-\mathrm{O} . \mathrm{D} .\) tube that is surrounded by a concentric tube of \(5 \mathrm{~cm}\) I.D. The inner and outer tubes are at \(800 \mathrm{~K}\) and \(500 \mathrm{~K}\), respectively, and the space between is evacuated. The outer surface of the inner tube has an emittance of \(0.15\), and the inner surface of the outer tube has an emittance of \(0.25\). Calculate the heat flow per unit length for the following situations: (i) The inner tube surface is a diffuse reflector and the outer tube surface is a specular reflector. (ii) The inner tube surface is a specular reflector and the outer tube surface is a diffuse reflector. athrm{~K}$.

A solar heater for a swimming pool consists of an unglazed copper plate \(0.5 \mathrm{~mm}\) thick with a selective coating (solar absorptance \(=0.92\), total hemispherical emittance \(=0.15\) ). On the back side of the plate are attached \(12 \mathrm{~mm}-\mathrm{O} . \mathrm{D} ., 1\) mm-wall-thickness copper tubes that are manifolded at the inlet and outlet to form a parallel tube matrix. The tubes have a centerline spacing of \(20 \mathrm{~cm}\) and make perfect thermal contact with the plate. Water at \(25^{\circ} \mathrm{C}\) is constantly recirculated from the pool at a flow rate per tube of \(0.5\) gallons/minute. On a given day the air temperature is \(20^{\circ} \mathrm{C}\), the air speed averages \(4 \mathrm{~m} / \mathrm{s}\) across a \(3 \mathrm{~m}\)-wide array of solar collectors, the solar irradiation is \(790 \mathrm{~W} / \mathrm{m}^{2}\), and the long wavelength radiation from the sky is about \(340 \mathrm{~W} / \mathrm{m}^{2}\). Determine the tube length required to supply water back to the pool at \(29^{\circ} \mathrm{C}\). Assume that the heat loss due to conduction through the back insulation is \(5 \%\) of the solar irradiation. Take \(\operatorname{Re}_{t r}=10^{5}\). (Hint: Appropriate assumptions will allow an analytical solution to be obtained.)

A thermistor is used to measure the temperature of a low-density helium flow. It is located in a \(10 \mathrm{~cm}\)-diameter tube through which the gas flows at \(1.6 \mathrm{~m} / \mathrm{s}\). The thermistor can be modeled as a \(3 \mathrm{~mm}\)-diameter sphere of emittance \(0.8\) and is located inside a radiation shield in the form of a \(1 \mathrm{~cm}\)-diameter, \(5 \mathrm{~cm}\)-long tube of emittance \(0.08\) (the axis of the tube is in the flow direction). If the thermistor records a temperature of \(327.5^{\circ} \mathrm{C}\) when the tube walls are at \(285^{\circ} \mathrm{C}\), determine the true temperature of the helium. Convective heat transfer coefficients on the thermistor and shield can be taken as \(19 \mathrm{~W} / \mathrm{m}^{2} \mathrm{~K}\) and \(5 \mathrm{~W} / \mathrm{m}^{2} \mathrm{~K}\), respectively. (Hint: First estimate the shield temperature.)

A small spherical thermocouple is located in the center of an open-ended circular tube of length \(H\) and radius \(R\). Determine the shape factor for radiation transfer between the thermocouple and the inside wall of the tube.

Calculate the equilibrium temperature of a small, flat plate with its top face exposed to an unobstructed view of the sky while air at \(298 \mathrm{~K}, 1 \mathrm{~atm}\) and \(20 \%\) relative humidity flows along both sides. The bottom face sees black surroundings at \(298 \mathrm{~K}\). The solar irradiation is \(800 \mathrm{~W} / \mathrm{m}^{2}\), and the average convective heat transfer coefficient is \(20 \mathrm{~W} / \mathrm{m}^{2} \mathrm{~K}\). Obtain solutions for three different kinds of surfaces: (i) Representative of a very white paint, \(\alpha_{s}=0.2, \varepsilon=0.9\) (ii) A metallic paint (aluminum), \(\alpha_{s}=0.3, \varepsilon=0.3\) (iii) A black paint, \(\alpha_{s}=0.9, \varepsilon=0.9\)

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