Warning: foreach() argument must be of type array|object, bool given in /var/www/html/web/app/themes/studypress-core-theme/template-parts/header/mobile-offcanvas.php on line 20

Two very large parallel plates are maintained at uniform temperatures of \(T_{1}=1100 \mathrm{~K}\) and \(T_{2}=700 \mathrm{~K}\) and have emissivities of \(\varepsilon_{1}=\varepsilon_{2}=0.5\), respectively. It is desired to reduce the net rate of radiation heat transfer between the two plates to one-fifth by placing thin aluminum sheets with an emissivity of \(0.1\) on both sides between the plates. Determine the number of sheets that need to be inserted.

Short Answer

Expert verified
Based on the information given, calculate the number of aluminum sheets needed to be inserted between the parallel plates to reduce the net radiation heat transfer to one-fifth of its initial value. Use the given emissivities and temperatures, as well as the Stefan-Boltzmann constant to determine the initial heat transfer rate, the desired heat transfer rate, and finally the number of aluminum sheets required to achieve the heat transfer reduction.

Step by step solution

01

Understand the initial heat transfer between the plates.

Using the equation of radiative exchange between parallel surfaces, the initial heat transfer can be calculated, given by: $$q_{1,2} = A\frac{\sigma(T_1^4 - T_2^4)}{\frac{1}{\varepsilon_1}+\frac{1}{\varepsilon_2}-1}$$ Here, \(A\) is the surface area of the parallel plates, \(\sigma\) is the Stefan-Boltzmann constant, and temperatures are in Kelvin.
02

Calculate the initial heat transfer rate.

First, let's calculate the initial heat transfer rate between the two given plates, using the emissivities and temperatures: $$q_{1,2} = A\frac{(5.67\times10^{-8}\mathrm{W}/\mathrm{m}^2\mathrm{K}^4)(1100^4 - 700^4)}{\frac{1}{0.5}+\frac{1}{0.5}-1}$$
03

Calculate the desired heat transfer rate

Now, as we want to reduce the heat transfer rate to one-fifth of the initial value, the desired heat transfer rate would be: $$q_{\text{desired}} = \frac{1}{5}q_{1,2}$$
04

Use the method of view factors.

To determine the number of aluminum sheets required, let's use the method of view factors \(F_{1,i}\) for parallel surfaces. We take the view factor from plate 1 to the i-th aluminum sheet as \(F_{1, i}\). The view factor from plate 1 to plate 2 is \(1\) since they are parallel surfaces. We can write the view factors in terms of the emissivities of aluminum sheets and the number of sheets, as follows: $$1 = \sum_{i=1}^n\varepsilon_iF_{1,i} + F_{1,2}$$, where \(n\) is the number of aluminum sheets.
05

Determine the heat transfer rate with aluminum sheets.

With the aluminum sheets between the plates, the heat transfer rate can be written as: $$q_{\text{desired}} = A\sum_{i=1}^n\frac{\sigma(T_1^4 - T_2^4)}{\frac{1}{\varepsilon_{1}}+\frac{1}{\varepsilon_{i}}-1}F_{1,i}$$ Now, we want to find the smallest integer \(n\) such that the desired heat transfer rate is one-fifth of the initial heat transfer rate.
06

Calculate the number of aluminum sheets.

Now, we need to find the number of aluminum sheets \(n\) necessary for the desired heat transfer rate: $$n = \left\lceil\frac{q_{1,2}}{5\left(\frac{\sigma(T_1^4 - T_2^4)}{\frac{1}{\varepsilon_{1}}+\frac{1}{0.1}-1}\right)}\right\rceil$$ We use the ceiling function \(\lceil \cdot \rceil\) to find the smallest integer value for \(n\). After calculating the values, we find the number of aluminum sheets required to reduce the heat transfer rate to one-fifth of its initial value.

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

A furnace is shaped like a long equilateral-triangular duct where the width of each side is \(2 \mathrm{~m}\). Heat is supplied from the base surface, whose emissivity is \(\varepsilon_{1}=0.8\), at a rate of $800 \mathrm{~W} / \mathrm{m}^{2}\( while the side surfaces, whose emissivities are \)0.4$, are maintained at \(600 \mathrm{~K}\). Neglecting the end effects, determine the temperature of the base surface. Can you treat this geometry as a two-surface enclosure?

Consider a \(10-\mathrm{ft} \times 10-\mathrm{ft} \times 10-\mathrm{ft}\) cubical furnace whose top and side surfaces closely approximate black surfaces and whose base surface has an emissivity \(\varepsilon=0.4\). The base, top, and side surfaces of the furnace are maintained at uniform temperatures of $800 \mathrm{R}, 1600 \mathrm{R}\(, and \)2400 \mathrm{R}$, respectively. Determine the net rate of radiation heat transfer between \((a)\) the base and the side surfaces and \((b)\) the base and the top surfaces. Also, determine the net rate of radiation heat transfer to the base surface.

A row of tubes, equally spaced at a distance that is twice the diameter of the tubes, is positioned between two large parallel plates. The surface temperature of the tubes is constant at \(10^{\circ} \mathrm{C}\) and the top and bottom plates are at constant temperatures of \(100^{\circ} \mathrm{C}\) and \(350^{\circ} \mathrm{C}\), respectively. If the surfaces behave as blackbody, determine the net radiation heat flux leaving the bottom plate.

Consider a \(3-\mathrm{m} \times 3-\mathrm{m} \times 3-\mathrm{m}\) cubical furnace. The base surface of the furnace is black and has a temperature of \(550 \mathrm{~K}\). The radiosities for the top and side surfaces are calculated to be \(7500 \mathrm{~W} / \mathrm{m}^{2}\) and $3200 \mathrm{~W} / \mathrm{m}^{2}$, respectively. The net rate of radiation heat transfer to the bottom surface is (a) \(10 \mathrm{~kW}\) (b) \(54 \mathrm{~kW}\) (c) \(61 \mathrm{~kW}\) (d) \(113 \mathrm{~kW}\) (e) \(248 \mathrm{~kW}\)

Consider a 30-cm-diameter hemispherical enclosure. The dome is maintained at \(600 \mathrm{~K}\), and heat is supplied from the dome at a rate of $65 \mathrm{~W}\( while the base surface with an emissivity of \)0.55$ is maintained at \(400 \mathrm{~K}\). Determine the emissivity of the dome.

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free