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Consider steady one-dimensional heat transfer through a plane wall exposed to convection from both sides to environments at known temperatures $T_{\infty 1}\( and \)T_{\infty 2}\( with known heat transfer coefficients \)h_{1}$ and \(h_{2}\). Once the rate of heat transfer \(\dot{Q}\) has been evaluated, explain how you would determine the temperature of each surface.

Short Answer

Expert verified
Answer: To find the heat transfer rate, first calculate the overall thermal resistance in the system, then use energy balance and temperature difference to get the heat transfer rate. Next, use convective heat transfer formulas to find the temperatures of each surface.

Step by step solution

01

Understand the problem components and variables

In this problem, consider the heat transfer through a plane wall as steady one-dimensional. The wall is exposed to convection from both sides, with known environment temperatures \(T_{\infty 1}\) and \(T_{\infty 2}\), and known heat transfer coefficients \(h_1\) and \(h_2\). Also, let the temperature of the wall surfaces be \(T_1\) and \(T_2\). We need to determine the rate of heat transfer \(\dot{Q}\) and explain how to find the temperature of each surface.
02

Apply the formula for the heat transfer rate

In order to determine the rate of heat transfer, we can apply the formula for the overall thermal resistance (\(R_{total}\)) in a one-dimensional conduction problem: \[R_{total} = \frac{1}{h_{1}A} + \frac{L}{kA} + \frac{1}{h_{2}A}\] Where \(A\) is the surface area, \(L\) is the thickness of the wall, and \(k\) is the wall's thermal conductivity. Now, using the energy balance and given \(\Delta T = T_{\infty 1} - T_{\infty 2}\), we can determine the heat transfer rate \(\dot{Q}\) as follows: \[\dot{Q} = \frac{\Delta T}{R_{total}}\]
03

Determine surface temperatures using the convective heat transfer formula

Now that we know the heat transfer rate, we can determine the temperatures of both surfaces. Let's examine the convective heat transfer from the surface at \(T_1\) to the environment with temperature \(T_{\infty 1}\). We can write the heat transfer rate as follows: \[\dot{Q} = h_{1}A(T_{1} - T_{\infty 1})\] Solving for \(T_1\): \[T_1 = \frac{\dot{Q}}{h_{1}A} + T_{\infty 1}\] Similarly, let's examine the convective heat transfer from the surface at \(T_2\) to the environment with temperature \(T_{\infty 2}\). We can write the heat transfer rate as follows: \[\dot{Q} = h_{2}A(T_{\infty 2} - T_{2})\] Solving for \(T_2\): \[T_2 = T_{\infty 2} - \frac{\dot{Q}}{h_{2}A}\] By first evaluating the heat transfer rate and then using convective heat transfer formulas, we are able to find the temperature of each surface, \(T_1\) and \(T_2\), in this steady one-dimensional heat transfer problem.

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Most popular questions from this chapter

A \(3-\mathrm{cm}\)-long, \(2-\mathrm{mm} \times 2-\mathrm{mm}\) rectangular cross-section aluminum fin \((k=237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) is attached to a surface. If the fin efficiency is 65 percent, the effectiveness of this single fin is (a) 39 (b) 30 (c) 24 (d) 18 (e) 7

Hot water $\left(c_{p}=4.179 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( flows through an 80 -m-long PVC \)(k=0.092 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\( pipe whose inner diameter is \)2 \mathrm{~cm}$ and outer diameter is \(2.5 \mathrm{~cm}\) at a rate of $1 \mathrm{~kg} / \mathrm{s}\(, entering at \)40^{\circ} \mathrm{C}$. If the entire interior surface of this pipe is maintained at \(35^{\circ} \mathrm{C}\) and the entire exterior surface at \(20^{\circ} \mathrm{C}\), the outlet temperature of water is (a) \(35^{\circ} \mathrm{C}\) (b) \(36^{\circ} \mathrm{C}\) (c) \(37^{\circ} \mathrm{C}\) (d) \(38^{\circ} \mathrm{C}\) (e) \(39^{\circ} \mathrm{C}\)

Circular fins of uniform cross section, with diameter of \(10 \mathrm{~mm}\) and length of \(50 \mathrm{~mm}\), are attached to a wall with surface temperature of \(350^{\circ} \mathrm{C}\). The fins are made of material with thermal conductivity of \(240 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), they are exposed to an ambient air condition of \(25^{\circ} \mathrm{C}\), and the convection heat transfer coefficient is $250 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Determine the heat transfer rate and plot the temperature variation of a single fin for the following boundary conditions: (a) Infinitely long fin (b) Adiabatic fin tip (c) Fin with tip temperature of \(250^{\circ} \mathrm{C}\) (d) Convection from the fin tip

A 2.2-mm-diameter and 14-m-long electric wire is tightly wrapped with a \(1-\mathrm{mm}\)-thick plastic cover whose thermal conductivity is $k=0.15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. Electrical measurements indicate that a current of \(13 \mathrm{~A}\) passes through the wire, and there is a voltage drop of \(8 \mathrm{~V}\) along the wire. If the insulated wire is exposed to a medium at \(T_{\infty}=30^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(h=24 \mathrm{~W} / \mathrm{m}^{2}\), \(\mathrm{K}\), determine the temperature at the interface of the wire and the plastic cover in steady operation. Also determine if doubling the thickness of the plastic cover will increase or decrease this interface temperature.

A triangular-shaped fin on a motorcycle engine is \(0.5 \mathrm{~cm}\) thick at its base and \(3 \mathrm{~cm}\) long (normal distance between the base and the tip of the triangle), and is made of aluminum $(k=150 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$. This fin is exposed to air with a convective heat transfer coefficient of \(30 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) acting on its surfaces. The efficiency of the fin is 75 percent. If the fin base temperature is \(130^{\circ} \mathrm{C}\) and the air temperature is $25^{\circ} \mathrm{C}$, the heat transfer from this fin per unit width is (a) \(32 \mathrm{~W} / \mathrm{m}\) (b) \(57 \mathrm{~W} / \mathrm{m}\) (c) \(102 \mathrm{~W} / \mathrm{m}\) (d) \(124 \mathrm{~W} / \mathrm{m}\) (e) \(142 \mathrm{~W} / \mathrm{m}\)

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