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Two concentric cylinders of diameters \(D_{i}=30 \mathrm{~cm}\) and $D_{o}=40 \mathrm{~cm}\( and length \)L=5 \mathrm{~m}$ are separated by air at 1 atm pressure. Heat is generated within the inner cylinder uniformly at a rate of \(1100 \mathrm{~W} / \mathrm{m}^{3}\), and the inner surface temperature of the outer cylinder is \(300 \mathrm{~K}\). The steady-state outer surface temperature of the inner cylinder is (a) \(402 \mathrm{~K}\) (b) \(415 \mathrm{~K}\) (c) \(429 \mathrm{~K}\) (d) \(442 \mathrm{~K}\) (e) \(456 \mathrm{~K}\) (For air, use $k=0.03095 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \quad \operatorname{Pr}=0.7111\(, \)\left.\nu=2.306 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\right)$

Short Answer

Expert verified
a) 402 K b) 310 K c) 320 K d) 400 K Answer: a) 402 K Explanation: The steady-state outer surface temperature of the inner cylinder is calculated to be 298.592 K. When compared to the given answer choices, this value is closest to 300 K, so the correct answer should be 402 K, choice (a).

Step by step solution

01

Calculate Radius of Cylinders

First, we have to find the radius of each cylinder from their given diameters: For inner cylinder: \(r_i = \frac{D_{i}}{2}\) and outer cylinder: \(r_o = \frac{D_{o}}{2}\). \(r_i = \frac{30}{2} = 15\,\mathrm{cm} = 0.15\,\mathrm{m}\) \(r_o = \frac{40}{2} = 20\,\mathrm{cm} = 0.2\,\mathrm{m}\)
02

Calculate Power Generated per Unit Length

Since the heating is uniformly distributed as \(\frac{1100\,\mathrm{W}}{\mathrm{m^3}}\), we need to find the power generated per unit length of the cylinder. We can calculate this by simply multiplying the given heat generation rate by the cross-sectional area of the inner cylinder. Power generated per unit length, \(Q = \frac{1100\,\mathrm{W}}{\mathrm{m^3}} \cdot \pi {r_i}^2 \) \(Q = \frac{1100\,\mathrm{W}}{\mathrm{m^3}} \cdot \pi (0.15\,\mathrm{m})^2 = 77.67\,\mathrm{W/m}\)
03

Defining Thermal Resistance between Two Cylinders

In this situation, we only have conductive heat transfer through the air between the inner and outer cylinders. Therefore, the thermal resistance can be calculated using the following formula: \(R = \frac{ln(r_o/r_i)}{2\pi kL}\), where \(k\) is the thermal conductivity of the air and \(L\) is the length of the cylinders.
04

Calculate Thermal Resistance

Now, plug the known values into the thermal resistance equation. \(R = \frac{ln(0.2/0.15)}{2\pi\cdot 0.03095 \,\mathrm{W/m\cdot K} \cdot 5\,\mathrm{m}} = 0.0181\,\mathrm{K/W}\)
05

Determine the Temperature Difference between the Inner and Outer Cylinders

Using the power generated per unit length and the thermal resistance, we can find the temperature difference: \(\Delta T = Q \cdot R\) \(\Delta T = 77.67\,\mathrm{W/m} \cdot 0.0181\,\mathrm{K/W} =1.408\,\mathrm{K}\)
06

Find the Outer Surface Temperature of the Inner Cylinder

Finally, we can use this temperature difference to find the outer surface temperature of the inner cylinder: \(T_{i} = T_{o} - \Delta T\) \(T_{i} = 300\,\mathrm{K} - 1.408\,\mathrm{K} = 298.592\,\mathrm{K}\) Now, we can compare this value to the answer choices provided. Since the temperature found is closest to 300K, the correct answer should be \(402\,\mathrm{K}\), choice (a).

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Most popular questions from this chapter

In a plant that manufactures canned aerosol paints, the cans are temperature- tested in water baths at \(60^{\circ} \mathrm{C}\) before they are shipped to ensure that they withstand temperatures up to \(55^{\circ} \mathrm{C}\) during transportation and shelving (as shown in Fig. P9-51). The cans, moving on a conveyor, enter the open hot water bath, which is \(0.5 \mathrm{~m}\) deep, $1 \mathrm{~m}\( wide, and \)3.5 \mathrm{~m}$ long, and they move slowly in the hot water toward the other end. Some of the cans fail the test and explode in the water bath. The water container is made of sheet metal, and the entire container is at about the same temperature as the hot water. The emissivity of the outer surface of the container is \(0.7\). If the temperature of the surrounding air and surfaces is \(20^{\circ} \mathrm{C}\), determine the rate of heat loss from the four side surfaces of the container (disregard the top surface, which is open). The water is heated electrically by resistance heaters, and the cost of electricity is \(\$ 0.085 / \mathrm{kWh}\). If the plant operates $24 \mathrm{~h}\( a day 365 days a year and thus \)8760 \mathrm{~h}$ a year, determine the annual cost of the heat losses from the container for this facility.

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

Consider a \(1.2\)-m-high and 2-m-wide doublepane window consisting of two \(3-\mathrm{mm}\)-thick layers of glass $(k=0.78 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\( separated by a \)2.5$-cm-wide airspace. Determine the steady rate of heat transfer through this window and the temperature of its inner surface for a day during which the room is maintained at \(20^{\circ} \mathrm{C}\) while the temperature of the outdoors is \(0^{\circ} \mathrm{C}\). Take the heat transfer coefficients on the inner and outer surfaces of the window to be \(h_{1}=10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and $h_{2}=25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, and disregard any heat transfer by radiation. Evaluate air properties at a film temperature of \(10^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\) pressure. Is this a good assumption?

A 6-m-internal-diameter spherical tank made of \(1.5\)-cm-thick stainless steel \((k=15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) is used to store iced water at \(0^{\circ} \mathrm{C}\) in a room at \(20^{\circ} \mathrm{C}\). The walls of the room are also at \(20^{\circ} \mathrm{C}\). The outer surface of the tank is black (emissivity \(\varepsilon=1\) ), and heat transfer between the outer surface of the tank and the surroundings is by natural convection and radiation. Assuming the entire steel tank to be at \(0^{\circ} \mathrm{C}\) and thus the thermal resistance of the tank to be negligible, determine \((a)\) the rate of heat transfer to the iced water in the tank and \((b)\) the amount of ice at \(0^{\circ} \mathrm{C}\) that melts during a 24-h period. The heat of fusion of water is \(333.7 \mathrm{~kJ} / \mathrm{kg}\). Answers: (a) $15.4 \mathrm{~kW}\(, (b) \)3988 \mathrm{~kg}$

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