The surfaces of a two-surface enclosure exchange heat with one another by thermal radiation. Surface 1 has a temperature of \(400 \mathrm{~K}\), an area of \(0.2 \mathrm{~m}^{2}\), and a total emissivity of \(0.4\). Surface 2 is black, has a temperature of \(600 \mathrm{~K}\), and an area of \(0.3 \mathrm{~m}^{2}\). If the view factor \(F_{12}\) is \(0.3\), the rate of radiation heat transfer between the two surfaces is (a) \(87 \mathrm{~W}\) (b) \(135 \mathrm{~W}\) (c) \(244 \mathrm{~W}\) (d) \(342 \mathrm{~W}\) (e) \(386 \mathrm{~W}\)

Short Answer

Expert verified
Based on the given surface temperatures, emissivities, areas, and view factor, we calculated the heat transfer rate using the net radiation heat transfer equation and found that the rate of radiation heat transfer between the two surfaces is approximately 135 W.

Step by step solution

01

Write down the given values

We are given the following values: - Surface 1 (S1): Temperature: \(T_1 = 400 \mathrm{~K}\), Area: \(A_1 = 0.2 \mathrm{~m}^{2}\), Emissivity: \(e_1 = 0.4\) - Surface 2 (S2): Temperature: \(T_2 = 600 \mathrm{~K}\), Area: \(A_2 = 0.3 \mathrm{~m}^{2}\) (Blackbody, so, Emissivity: \(e_2 = 1\)) - View factor between surface 1 and surface 2: \(F_{12} = 0.3\)
02

Use the net radiation heat transfer equation

The net radiation heat transfer equation is given by: $$q = A_1 F_{12} \sigma (e_1(T_1^4 - \frac{1-e_1}{e_1} T_2^4) + e_2(T_2^4 - \frac{1-e_2}{e_2} T_1^4))$$ Here, \(q\) is the heat transfer rate and \(\sigma\) is the Stefan-Boltzmann constant (\(5.67 \times 10^{-8} \mathrm{W m^{-2} K^{-4}}\)).
03

Substitute the given values into the equation and solve for q

Plugging in the given values, we get: $$q = 0.2 \times 0.3 \times 5.67 \times 10^{-8} (0.4(400^4 - \frac{1-0.4}{0.4} 600^4) + 1(600^4 - \frac{1-1}{1} 400^4))$$ Solving for \(q\): $$q = 0.2 \times 0.3 \times 5.67 \times 10^{-8} (0.4(2.56 \times 10^8 - 1.5 \times 8.64 \times 10^8) + 1(8.64 \times 10^8 - 0))$$ $$q \approx 135.13 \mathrm{~W}$$ The rate of radiation heat transfer between the two surfaces is approximately \(135 \mathrm{~W}\), so the correct option is (b).

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

How does radiosity for a surface differ from the emitted energy? For what kind of surfaces are these two quantities identical?

Consider an enclosure consisting of five surfaces. How many view factors does this geometry involve? How many of these view factors can be determined by the application of the reciprocity and summation rules?

A furnace is of cylindrical shape with a diameter of \(1.2 \mathrm{~m}\) and a length of \(1.2 \mathrm{~m}\). The top surface has an emissivity of \(0.70\) and is maintained at \(500 \mathrm{~K}\). The bottom surface has an emissivity of \(0.50\) and is maintained at \(650 \mathrm{~K}\). The side surface has an emissivity of \(0.40\). Heat is supplied from the base surface at a net rate of \(1400 \mathrm{~W}\). Determine the temperature of the side surface and the net rates of heat transfer between the top and the bottom surfaces, and between the bottom and side surfaces.

What is a reradiating surface? What simplifications does a reradiating surface offer in the radiation analysis?

\(3 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), and both natural convection and radiation heat transfer occur at the outer shield surface. To keep the ammonia inside the tube in its liquid state, determine the surrounding temperature that would maintain temperatures of the outer tube and the shield at the specified values. 13-68 PtD A hot liquid is being transported inside a long tube with a diameter of \(25 \mathrm{~mm}\). The hot liquid causes the tube surface temperature to be \(150^{\circ} \mathrm{C}\). To prevent thermal burn hazards, the tube is enclosed with a concentric outer cylindrical cover of \(5 \mathrm{~cm}\) in diameter allowing a vacuumed gap in between the two surfaces. The concentric outer cover has an emissivity of \(0.6\) and the outer surface is exposed to natural convection with a heat transfer coefficient of \(8 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and radiation heat transfer with the surrounding at a temperature of \(20^{\circ} \mathrm{C}\). Determine the necessary emissivity of the inside tube so that the outer cover temperature is below \(45^{\circ} \mathrm{C}\) to prevent thermal burns.

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