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 concentric spheres with diameters of \(5 \mathrm{~cm}\) and $10 \mathrm{~cm}\( have their surface temperatures maintained at \)100^{\circ} \mathrm{C}\( and \)200^{\circ} \mathrm{C}$, respectively. The enclosure between the two concentric spherical surfaces is filled with nitrogen gas at \(\mathrm{atm}\). Determine the rate of heat transfer through the enclosure.

Short Answer

Expert verified
Answer: The rate of heat transfer between the two concentric spheres filled with nitrogen gas is approximately 714.29 W.

Step by step solution

01

Identify the known variables and constants

We are given the following: - Inner sphere diameter: \(d_1 = 5 \mathrm{~cm}\) - Outer sphere diameter: \(d_2 = 10 \mathrm{~cm}\) - Inner sphere temperature: \(T_1 = 100^{\circ} \mathrm{C}\) - Outer sphere temperature: \(T_2 = 200^{\circ} \mathrm{C}\) - The gas is nitrogen at atmospheric pressure. We need to find the thermal conductivity of nitrogen gas, which is approximately \(k_{N_2} = 0.024 \mathrm{~W/m\cdot K}\) at room temperature and atmospheric pressure.
02

Calculate the radii of the spheres and the temperature difference

First, let's find the radii \(r_1\) and \(r_2\) of the inner and outer spheres by dividing the diameters by 2. \(r_1 = \frac{d_1}{2} = 2.5 \mathrm{~cm}\) \(r_2 = \frac{d_2}{2} = 5 \mathrm{~cm}\) For simplicity, we can convert the radii to meters. \(r_1 = 0.025 \mathrm{~m}\) \(r_2 = 0.05 \mathrm{~m}\) Now let's find the temperature difference between the spheres in Kelvin. \(\Delta T = T_2 - T_1 = 200 - 100 = 100 \mathrm{~K}\)
03

Calculate the thermal resistance of the gas-filled enclosure

The thermal resistance for concentric spheres is given by the following equation: \(R_{enclosure} = \frac{1}{4\pi k_{N_2}}\left(\frac{1}{r_1} - \frac{1}{r_2}\right)\) Plug in the values to calculate the thermal resistance: \(R_{enclosure} = \frac{1}{4\pi (0.024)}\left(\frac{1}{0.025} - \frac{1}{0.05}\right) \approx 0.14 \mathrm{~m \cdot K/W}\)
04

Determine the rate of heat transfer

Now that we have the thermal resistance, we can calculate the rate of heat transfer using the following equation: \(q = \frac{\Delta T}{R_{enclosure}}\) Plug in the values: \(q = \frac{100 \mathrm{~K}}{0.14 \mathrm{~m \cdot K/W}} \approx 714.29 \mathrm{~W}\) Therefore, the rate of heat transfer through the enclosure is approximately \(714.29 \mathrm{~W}\).

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

Consider a double-pane window whose airspace is flashed and filled with argon gas. How will replacing the air in the gap with argon affect \((a)\) convection and \((b)\) radiation heat transfer through the window?

Consider an industrial furnace that resembles a 13-ft-long horizontal cylindrical enclosure \(8 \mathrm{ft}\) in diameter whose end surfaces are well insulated. The furnace burns natural gas at a rate of 48 therms/h. The combustion efficiency of the furnace is 82 percent (i.e., 18 percent of the chemical energy of the fuel is lost through the flue gases as a result of incomplete combustion and the flue gases leaving the furnace at high temperature). If the heat loss from the outer surfaces of the furnace by natural convection and radiation is not to exceed 1 percent of the heat generated inside, determine the highest allowable surface temperature of the furnace. Assume the air and wall surface temperature of the room to be \(75^{\circ} \mathrm{F}\), and take the emissivity of the outer surface of the furnace to be \(0.85\).

Consider an \(L \times L\) horizontal plate that is placed in quiescent air with the hot surface facing up. If the film temperature is \(20^{\circ} \mathrm{C}\) and the average Nusselt number in natural convection is of the form \(\mathrm{Nu}=C \mathrm{Ra}_{L}^{n}\), show that the average heat transfer coefficient can be expressed as $$ \begin{array}{ll} h=1.95(\Delta T / L)^{1 / 4} & 10^{4}<\mathrm{Ra}_{L}<10^{7} \\ h=1.79 \Delta T^{1 / 3} & 10^{7}<\mathrm{Ra}_{L}<10^{11} \end{array} $$

A \(0.2-\mathrm{m}\)-long and \(25-\mathrm{mm}\)-thick vertical plate $(k=1.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$ separates the hot water from the cold air at \(2^{\circ} \mathrm{C}\). The plate surface exposed to the hot water has a temperature of \(100^{\circ} \mathrm{C}\), and the surface exposed to the cold air has an emissivity of \(0.73\). Determine the temperature of the plate surface exposed to the cold air \(\left(T_{s, c}\right)\). Hint: The \(T_{s, c}\) has to be found iteratively. Start the iteration process with an initial guess of \(51^{\circ} \mathrm{C}\) for the \(T_{s, c^{*}}\)

A hot object suspended by a string is to be cooled by natural convection in fluids whose volume changes differently with temperature at constant pressure. In which fluid will the rate of cooling be lowest? With increasing temperature, a fluid whose volume (a) increases a lot (b) increases slightly (c) does not change (d) decreases slightly (e) decreases a lot

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