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A 30 -cm-diameter black ball at \(120^{\circ} \mathrm{C}\) is suspended in air. It is losing heat to the surrounding air at \(25^{\circ} \mathrm{C}\) by convection with a heat transfer coefficient of $12 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$ and by radiation to the surrounding surfaces at \(15^{\circ} \mathrm{C}\). The total rate of heat transfer from the black ball is (a) \(322 \mathrm{~W}\) (b) \(595 \mathrm{~W}\) (c) \(234 \mathrm{~W}\) (d) \(472 \mathrm{~W}\) (e) \(2100 \mathrm{~W}\)

Short Answer

Expert verified
Answer: The approximate total rate of heat transfer is 918.79 W.

Step by step solution

01

Understand given information

We are given the diameter of the black ball (\(D = 30 cm\) or \(0.3 m\)), the temperature of the black ball (\(T_{ball} = 120^{\circ} \mathrm{C}\)), the surrounding air temperature (\(T_{air} = 25^{\circ} \mathrm{C}\)), and the heat transfer coefficient by convection (\(h = 12 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\)). The temperature of the surrounding surfaces is \(T_{surfaces} = 15^{\circ} \mathrm{C}\).
02

Calculate the ball's surface area

To find the surface area of the ball, we can use the formula \(A = 4 \pi r^{2}\), where \(r\) is the ball's radius. The radius can be found by dividing the diameter by 2: \(r = 0.3 m / 2 = 0.15 m\). Thus, the surface area is \(A = 4 \pi (0.15)^{2} = 0.2827 \mathrm{~m}^{2}\).
03

Calculate the rate of convective heat transfer

We can calculate the rate of convective heat transfer with the formula \(Q_{conv} = hA(T_{ball} - T_{air})\). Convert the temperatures to Kelvin: \(T_{ball} = 120 + 273.15 = 393.15 \mathrm{K}\) and \(T_{air} = 25 +273.15 =298.15 \mathrm{K}\). Now, \(Q_{conv} = 12 \times 0.2827 (393.15 - 298.15) = 321.61 \mathrm{~W}\).
04

Calculate the rate of radiative heat transfer

To calculate the rate of radiative heat transfer, we can use the formula \(Q_{rad} = \sigma \epsilon A (T_{ball}^{4} - T_{surfaces}^{4})\), where \(\sigma\) is the Stefan-Boltzmann constant (\(5.67 \times 10^{-8} \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}^{4}\)), \(\epsilon\) is the emissivity of the black ball (\(\epsilon = 1\) for a perfect black body), and \(T_{surfaces}\) is the temperature of the surrounding surfaces. Convert \(T_{surfaces}\) to Kelvin: \(T_{surfaces} = 15 + 273.15 = 288.15 \mathrm{K}\). Now, \(Q_{rad} = 5.67 \times 10^{-8} \times 1 \times 0.2827 (393.15^{4} - 288.15^{4}) = 597.18 \mathrm{~W}\).
05

Calculate the total rate of heat transfer

Now we can calculate the total rate of heat transfer by adding the convective rate and the radiative rate: \(Q_{total} = Q_{conv} + Q_{rad} = 321.61 \mathrm{~W} + 597.18 \mathrm{~W} = 918.79 \mathrm{~W}\). However, none of the given options match this result. It's possible that there is an error in the problem's given choices, or some assumptions were made along the way that led to a different answer. Based on the calculations, the total rate of heat transfer would be approximately 918.79 W.

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Most popular questions from this chapter

Heat treatment of metals is commonly done using electrically heated draw batch furnaces. Consider a furnace that is situated in a room with a surrounding air temperature of \(30^{\circ} \mathrm{C}\) and an average convection heat transfer coefficient of \(15 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The outer furnace front surface has an emissivity of \(0.7\), and the inside surface is subjected to a heat flux of \(5 \mathrm{~kW} / \mathrm{m}^{2}\). To ensure safety and avoid thermal burns to people working around the furnace, the outer front surface of the furnace should be kept below \(50^{\circ} \mathrm{C}\). Based on the information given about the furnace, does the furnace front surface require insulation to prevent thermal burns?

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