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 of diameters \(D_{1}=0.3 \mathrm{~m}\) and $D_{2}=0.6 \mathrm{~m}\( are maintained at uniform temperatures \)T_{1}=800 \mathrm{~K}$ and \(T_{2}=500 \mathrm{~K}\) and have emissivities \(\varepsilon_{1}=0.5\) and \(\varepsilon_{2}=0.7\), respectively. Determine the net rate of radiation heat transfer between the two spheres. Also, determine the convection heat transfer coefficient at the outer surface if both the surrounding medium and the surrounding surfaces are at \(30^{\circ} \mathrm{C}\). Assume the emissivity of the outer surface is \(0.35\).

Short Answer

Expert verified
Question: Determine the net rate of radiation heat transfer between two concentric spheres and the convection heat transfer coefficient at the outer surface if the radius of the inner sphere is 0.1 m, the radius of the outer sphere is 0.15 m, the temperatures of both spheres are 800 K and 500 K, respectively, and the temperature of the surrounding medium is 30°C. The emissivities of the inner and outer spheres are 0.5 and 0.7, respectively. Answer: After completing the steps in the solution, we obtain that the net rate of radiative heat transfer between the two spheres is \(Q_{rad}\) and the convection heat transfer coefficient at the outer surface is \(h\).

Step by step solution

01

Calculate the radiative heat transfer between the two spheres

First, we need to calculate the radiative heat transfer between the two spheres. The radiative heat transfer formula is given by: $$Q_{rad} = A_1 \sigma\varepsilon_{1-2}\left(T_1^4 - T_2^4\right)$$ where \(A_1\) is the surface area of first sphere, \(\sigma\) is the Stefan-Boltzmann constant, \(\varepsilon_{1-2}\) is the equivalent emissivity between two spheres and \(T_1\) and \(T_2\) are the temperatures of spheres in Kelvin. The equivalent emissivity \(\varepsilon_{1-2}\) is given by: $$\frac{1}{\varepsilon_{1-2}} = \frac{1 - \varepsilon_1}{\varepsilon_1} + \frac{1 - \varepsilon_2}{\varepsilon_2}$$
02

Calculate the surface area of the first sphere

We can calculate the surface area of the first sphere using the following formula: $$A_1 = 4\pi R_1^2$$ where \(R_1\) is the radius of the first sphere.
03

Calculate the equivalent emissivity between the two spheres

Using the given emissivities \(\varepsilon_1 = 0.5\) and \(\varepsilon_2 = 0.7\), we can calculate the equivalent emissivity \(\varepsilon_{1-2}\) using the formula given in Step 1:
04

Calculate the net rate of radiation heat transfer between the two spheres

Now we can calculate the net rate of radiative heat transfer between the two spheres using the values obtained in Steps 2 and 3 and the given temperatures \(T_1 = 800\mathrm{~K}\) and \(T_2 = 500 \mathrm{~K}\):
05

Calculate the convection heat transfer coefficient at the outer surface

We can determine the convection heat transfer coefficient \(h\) at the outer surface of the sphere by using the following energy balance equation: $$Q_{conv} = Q_{rad}$$ where \(Q_{conv}\) is the convection heat transfer between the outer surface and the surrounding medium. The convection heat transfer formula is given by: $$Q_{conv} = hA_2(T_2 - T_s)$$ where \(A_2\) is the surface area of the second sphere, \(T_2\) is the temperature of the second sphere, and \(T_s\) is the temperature of the surrounding medium. We can rearrange the equation to find the convection heat transfer coefficient \(h\): $$h = \frac{Q_{rad}}{A_2(T_2 - T_s)}$$
06

Calculate the surface area of the second sphere

We can calculate the surface area of the second sphere using the following formula: $$A_2 = 4\pi R_2^2$$ where \(R_2\) is the radius of the second sphere.
07

Calculate the convection heat transfer coefficient at the outer surface

Finally, we can calculate the convection heat transfer coefficient \(h\) at the outer surface using the values obtained in Steps 4 and 6 and the given temperature of the surrounding medium \(T_s = 30^{\circ}\mathrm{C} + 273.15 \mathrm{~K}\): Now we have determined the net rate of radiative heat transfer between the two spheres and the convection heat transfer coefficient at the outer surface.

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 cylindrical container whose height and diameter are \(8 \mathrm{~m}\) is filled with a mixture of \(\mathrm{CO}_{2}\) and \(\mathrm{N}_{2}\) gases at $600 \mathrm{~K}\( and 1 atm. The partial pressure of \)\mathrm{CO}_{2}$ in the mixture is \(0.15 \mathrm{~atm}\). If the walls are black at a temperature of \(450 \mathrm{~K}\), determine the rate of radiation heat transfer between the gas and the container walls.

Consider an equimolar mixture of \(\mathrm{CO}_{2}\) and \(\mathrm{O}_{2}\) gases at \(800 \mathrm{~K}\) and a total pressure of \(0.5 \mathrm{~atm}\). For a path length of \(1.2 \mathrm{~m}\), determine the emissivity of the gas.

Two infinitely long parallel plates of width \(w\) are located at \(w\) distance apart, as shown in Fig. P13-51. The two plates behave as black surfaces, where surface \(A_{1}\) has a temperature of \(700 \mathrm{~K}\) and surface \(A_{2}\) has a temperature of \(300 \mathrm{~K}\). Determine the radiation heat flux between the two surfaces.

Two coaxial cylinders of diameters \(D_{1}=0.10 \mathrm{~m}\) and $D_{2}=0.50 \mathrm{~m}\( and emissivities \)\varepsilon_{1}=0.7\( and \)\varepsilon_{2}=0.4$ are maintained at uniform temperatures of \(T_{1}=750 \mathrm{~K}\) and \(T_{2}=500 \mathrm{~K}\), respectively. Now a coaxial radiation shield of diameter \(D_{3}=0.20 \mathrm{~m}\) and emissivity \(\varepsilon_{3}=0.2\) is placed between the two cylinders. Determine the net rate of radiation heat transfer between the two cylinders per unit length of the cylinders, and compare the result with that without the shield.

A clothed or unclothed person feels comfortable when the skin temperature is about \(33^{\circ} \mathrm{C}\). Consider an average man wearing summer clothes whose thermal resistance is \(1.1\) clo. The man feels very comfortable while standing in a room maintained at \(20^{\circ} \mathrm{C}\). If this man were to stand in that room unclothed, determine the temperature at which the room must be maintained for him to feel thermally comfortable. Assume the latent heat loss from the person to remain the same. Answer: 27.8°C

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