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To defog the rear window of an automobile, a very thin transparent heating element is attached to the inner surface of the window. A uniform heat flux of \(1300 \mathrm{~W} / \mathrm{m}^{2}\) is provided to the heating element for defogging a rear window with thickness of \(5 \mathrm{~mm}\). The interior temperature of the automobile is \(22^{\circ} \mathrm{C}\), and the convection heat transfer coefficient is $15 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. The outside ambient temperature is \)-5^{\circ} \mathrm{C}$, and the convection heat transfer coefficient is $100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. If the thermal conductivity of the window is \)1.2 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$, determine the inner surface temperature of the window.

Short Answer

Expert verified
Based on the provided information and using heat transfer concepts, the inner surface temperature of the rear window of an automobile is calculated to be approximately 12.1°C.

Step by step solution

01

Determine Heat Transfer through the Window

First, we need to determine the heat transfer through the window. We are given the heat flux and can thus calculate the total heat transfer by multiplying the heat flux by the area of the window. It is given by: $$Q =q''A$$ Here, we are only asked to find the inner surface temperature of the window, so we don't need to find the exact value for the heat transfer Q. The ratios will remain constant for the steps we're going to calculate.
02

Calculate Heat Transfer by Conduction

To find the inner surface temperature of the window, we first need to determine the heat transfer by conduction that occurs through the window. This can be calculated using Fourier's law: $$q''_{cond} = \frac{k(T_i - T_o)}{L}$$ Where \(q''_{cond}\) is the conductive heat flux, \(k\) is the thermal conductivity \((1.2 \ \mathrm{W / m \cdot K})\), \(T_i\) is the inner surface temperature of the window, \(T_o\) is the outer surface temperature of the window, and \(L\) is the thickness of the window \((5 \times 10^{-3} \ \mathrm{m})\).
03

Calculate Heat Transfer by Convection (Interiors and Exteriors)

Next, we need to determine the heat transfer by convection that occurs on both the inside and outside of the window. This can be calculated using Newton's law of cooling: $$q''_{conv,i} = h_i(T_{in} - T_i)$$ $$q''_{conv,o} = h_o(T_o - T_{amb})$$ Where \(q''_{conv,i}\) is the convective heat flux at the inner surface, \(q''_{conv,o}\) is the convective heat flux at the outer surface, \(h_i\) is the convection heat transfer coefficient for the interior \((15 \ \mathrm{W / m^2 \cdot K})\), \(h_o\) is the convection heat transfer coefficient for the exterior \((100 \ \mathrm{W / m^2 \cdot K})\), \(T_{in}\) is the interior temperature of the automobile \((22^\circ \ \mathrm{C})\), and \(T_{amb}\) is the outside ambient temperature \((-5^\circ \ \mathrm{C})\).
04

Combine the Equations and Solve for Inner Surface Temperature

At steady-state, the heat transfer through the convection processes equals the heat transfer through the conduction process. Therefore: $$q''_{cond} = q''_{conv,i} + q''_{conv,o}$$ Substituting the equations for heat transfer from steps 2 and 3 into the above equation and solving for the inner surface temperature, we get: $$\frac{k(T_i - T_o)}{L} = h_i(T_{in} - T_i) + h_o(T_o - T_{amb})$$ We know that \(q''_{cond} = q''\), so we get: $$\frac{k(T_i - T_o)}{L} = q''$$ Now, we substitute this back into the equation and solve for the inner surface temperature: $$q'' = h_i(T_{in} - T_i) + h_o \left(\frac{Lq''}{k} + T_i -T_{amb} \right)$$ Plugging in the given values and solving for \(T_i\), we find that the inner surface temperature of the window is approximately: $$T_i = 12.1^\circ \ \mathrm{C}$$

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Most popular questions from this chapter

A 1-m-inner-diameter liquid-oxygen storage tank at a hospital keeps the liquid oxygen at \(90 \mathrm{~K}\). The tank consists of a \(0.5\)-cm-thick aluminum \((k=170 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) shell whose exterior is covered with a 10 -cm-thick layer of insulation \((k=0.02\) $\mathrm{W} / \mathrm{m} \cdot \mathrm{K})$. The insulation is exposed to the ambient air at \(20^{\circ} \mathrm{C}\). and the heat transfer coefficient on the exterior side of the insulation is \(5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The temperature of the exterior surface of the insulation is (a) \(13^{\circ} \mathrm{C}\) (b) \(9^{\circ} \mathrm{C}\) (c) \(2^{\circ} \mathrm{C}\) \((d)-3^{\circ} \mathrm{C}\) \((e)-12^{\circ} \mathrm{C}\)

Using cylindrical samples of the same material, devise an experiment to determine the thermal contact resistance. Cylindrical samples are available at any length, and the thermal conductivity of the material is known.

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) \(2.5 \mathrm{~cm}\)

One wall of a refrigerated warehouse is \(10.0 \mathrm{~m}\) high and $5.0 \mathrm{~m}\( wide. The wall is made of three layers: \)1.0$-cm-thick aluminum \((k=200 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}), 8.0\)-cm-thick fiberglass \((k=0.038\) \(\mathrm{W} / \mathrm{m} \cdot \mathrm{K})\), and \(3.0\)-cm-thick gypsum board \((k=0.48 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\). The warehouse inside and outside temperatures are \(-10^{\circ} \mathrm{C}\) and \(20^{\circ} \mathrm{C}\), respectively, and the average value of both inside and outside heat transfer coefficients is \(40 \mathrm{~W} / \mathrm{m}^{2}\). \(\mathrm{K}\). (a) Calculate the rate of heat transfer across the warehouse wall in steady operation. (b) Suppose that 400 metal bolts ( $k=43 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\(, each \)2.0 \mathrm{~cm}\( in diameter and \)12.0 \mathrm{~cm}$ long, are used to fasten (i.e., hold together) the three wall layers. Calculate the rate of heat transfer for the "bolted" wall. (c) What is the percent change in the rate of heat transfer across the wall due to metal bolts?

An 8-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 \(0^{\circ} \mathrm{C}\). The tank is located in a room whose temperature is \(25^{\circ} \mathrm{C}\). The walls of the room are also at $25^{\circ} \mathrm{C}$. 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. The convection heat transfer coefficients at the inner and the outer surfaces of the tank are $80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\( and \)10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(, respectively. Determine \)(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 at atmospheric pressure is \(h_{i f}=333.7 \mathrm{~kJ} / \mathrm{kg}\).

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