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Consider a 3-m-high, 6-m-wide, and \(0.25\)-m-thick brick wall whose thermal conductivity is \(k=0.8 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). On a certain day, the temperatures of the inner and the outer surfaces of the wall are measured to be \(14^{\circ} \mathrm{C}\) and \(5^{\circ} \mathrm{C}\), respectively. Determine the rate of heat loss through the wall on that day.

Short Answer

Expert verified
Answer: The rate of heat loss through the wall is 259.2 W.

Step by step solution

01

Understand Fourier's Law of heat conduction

Fourier's law states that the rate of heat transfer through a material is proportional to the negative of the temperature gradient and the material's thermal conductivity. Mathematically, it is represented as: \(q = -kA\frac{\Delta T}{\Delta x} \) where, \(q\) = rate of heat transfer (W) \(k\) = thermal conductivity (W/mK) \(A\) = the area through which heat is transferred (m²) \(\Delta T\) = temperature difference between the two surfaces (K) \(\Delta x\) = thickness of the material (m)
02

Calculate the area of the wall

We are given the dimensions of the wall: 3 m height and 6 m width. To find the area through which heat is transferred, we multiply the height and width of the wall: \(A = 3\,\text{m} \times 6\,\text{m} = 18\,\text{m}^{2}\)
03

Calculate the temperature difference

We are given the temperatures of the inner and outer surfaces of the wall as \(14^{\circ} \mathrm{C}\) and \(5^{\circ} \mathrm{C}\), respectively. The temperature difference between the two surfaces is: \(\Delta T = T_{\text{inner}} - T_{\text{outer}} = 14^{\circ} \mathrm{C} - 5^{\circ} \mathrm{C} = 9\,\mathrm{K}\) Note that the temperature difference in Kelvin (K) is the same as the difference in Celsius.
04

Use the formula to find the rate of heat loss

Now, we have all the necessary values to calculate the rate of heat loss, also known as the rate of heat transfer, using Fourier's Law: \(q = -kA\frac{\Delta T}{\Delta x} \) Plug in the given values into the equation: \(q = -0.8\,\mathrm{W/mK} \times 18\,\text{m}^{2} \,\times \dfrac{9\,\mathrm{K}}{0.25\,\text{m}}\) Solve the expression: \(q = -259.2\,\text{W}\) Since the rate of heat loss is negative, it means that the heat is being transferred from the inner surface to the outer surface, which is expected as the inner surface has a higher temperature. The magnitude of the rate of heat loss, which is what the exercise asks for, is: \(q_{\text{loss}} = 259.2\, \mathrm{W}\) Therefore, the rate of heat loss through the wall on that day is 259.2 W.

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Most popular questions from this chapter

Hot water flows in a 1-m-long section of a pipe that is made of acrylonitrile butadiene styrene (ABS) thermoplastic. The \(\mathrm{ABS}\) pipe section has an inner diameter of \(D_{1}=22 \mathrm{~mm}\) and an outer diameter of $D_{2}=27 \mathrm{~mm}\(. The thermal conductivity of the ABS pipe wall is \)0.1 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. The outer pipe surface is exposed to convection heat transfer with air at \(20^{\circ} \mathrm{C}\) and $h=10 \mathrm{~W} / \mathrm{m}^{2} . \mathrm{K}$. The water flowing inside the pipe has a convection heat transfer coefficient of $50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. According to the ASME Code for Process Piping (ASME B31.3-2014, Table B-1), the maximum recommended temperature for \(\mathrm{ABS}\) pipe is \(80^{\circ} \mathrm{C}\). Determine the maximum temperature of the water flowing in the pipe, such that the ABS pipe is operating at the recommended temperature or lower. What is the temperature at the outer pipe surface when the water is at maximum temperature?

Hot air is to be cooled as it is forced to flow through the tubes exposed to atmospheric air. Fins are to be added in order to enhance heat transfer. Would you recommend attaching the fins inside or outside the tubes? Why? When would you recommend attaching fins both inside and outside the tubes?

Heat is generated steadily in a \(3-\mathrm{cm}\)-diameter spherical ball. The ball is exposed to ambient air at \(26^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(7.5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The ball is to be covered with a material of thermal conductivity $0.15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. The thickness of the covering material that will maximize heat generation within the ball while keeping ball surface temperature constant is (a) \(0.5 \mathrm{~cm}\) (b) \(1.0 \mathrm{~cm}\) (c) \(1.5 \mathrm{~cm}\) (d) \(2.0 \mathrm{~cm}\) (e) \(2.5 \mathrm{~cm}\)

A plane wall surface at \(200^{\circ} \mathrm{C}\) is to be cooled with aluminum pin fins of parabolic profile with blunt tips. Each fin has a length of $25 \mathrm{~mm}\( and a base diameter of \)4 \mathrm{~mm}$. The fins are exposed to ambient air at \(25^{\circ} \mathrm{C}\), and the heat transfer coefficient is \(45 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). If the thermal conductivity of the fins is 230 \(\mathrm{W} / \mathrm{m} \cdot \mathrm{K}\), determine the heat transfer rate from a single fin and the increase in the rate of heat transfer per \(\mathrm{m}^{2}\) surface area as a result of attaching fins. Assume there are 100 fins per \(\mathrm{m}^{2}\) surface area.

Computer memory chips are mounted on a finned metallic mount to protect them from overheating. A \(152-\mathrm{MB}\) memory chip dissipates \(5 \mathrm{~W}\) of heat to air at \(25^{\circ} \mathrm{C}\). If the temperature of this chip is not to exceed \(60^{\circ} \mathrm{C}\), the overall heat transfer coefficient- area product of the finned metal mount must be at least (a) \(0.14 \mathrm{~W} /{ }^{\circ} \mathrm{C}\) (b) \(0.20 \mathrm{~W} /{ }^{\circ} \mathrm{C}\) (c) \(0.32 \mathrm{~W} /{ }^{\circ} \mathrm{C}\) (d) \(0.48 \mathrm{~W} /{ }^{\circ} \mathrm{C}\) (e) \(0.76 \mathrm{~W} /{ }^{\circ} \mathrm{C}\)

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