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Consider steady heat transfer through the wall of a room in winter. The convection heat transfer coefficient at the outer surface of the wall is three times that of the inner surface as a result of the winds. On which surface of the wall do you think the temperature will be closer to the surrounding air temperature? Explain.

Short Answer

Expert verified
Answer: In winter, the outer surface of the wall will have a temperature closer to the surrounding air temperature.

Step by step solution

01

Introduce convection heat transfer coefficients

A convection heat transfer coefficient is the ratio of heat transferred between a solid surface and a fluid to the temperature difference between the surface and the fluid. In this problem, we are given the information that the convection heat transfer coefficient at the outer surface of the wall is three times that of the inner surface due to winds. Let h_in denote the convection heat transfer coefficient of the inner surface and h_out denote the convection heat transfer coefficient of the outer surface. So, we have: h_out = 3 * h_in
02

Define temperature variables

Let's use the following notation for the temperatures: T_in = temperature at the inner surface of the wall, T_out = temperature at the outer surface of the wall, T_room = temperature of the room (inside), and T_air = temperature of the air outside.
03

Apply the convection heat transfer equation

For steady heat transfer through the wall, the heat transfer rate along the wall should be constant. We can use the convection heat transfer equation given by: Q_cond = Q_conv where, Q_cond - heat transfer rate by conduction through the wall, Q_conv - heat transfer rate by convection from the inner surface to the room and the outer surface to the air outside. Using the convection heat transfer equation, we can write: Q_conv_in = h_in * A * (T_room - T_in) Q_conv_out = h_out * A * (T_out - T_air) Considering steady heat transfer, Q_conv_in = Q_conv_out.
04

Calculate temperature differences

Using the information given, we can find the temperature difference between the inner and outer surfaces of the wall and the surrounding air temperatures. Since h_out = 3 * h_in and they are equal: h_in * A * (T_room - T_in) = 3 * h_in * A * (T_out - T_air) By canceling out h_in and A, we get: (T_room - T_in) = 3 * (T_out - T_air)
05

Determine which surface is closer to surrounding air temperature

Considering the relationship derived in Step 4, we can now determine which surface has a temperature closer to the surrounding air temperature. In winter, T_room > T_air, so (T_room - T_in) > (T_out - T_air). Since the temperature difference between the inner surface and the room is greater than the temperature difference between the outer surface and the air outside, the temperature of the outer surface is closer to the surrounding air temperature. Thus, the temperature at the outer surface of the wall is closer to the surrounding air temperature.

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Most popular questions from this chapter

Consider a very long rectangular fin attached to a flat surface such that the temperature at the end of the fin is essentially that of the surrounding air, i.e., \(20^{\circ} \mathrm{C}\). Its width is \(5.0 \mathrm{~cm}\); thickness is \(1.0 \mathrm{~mm}\); thermal conductivity is $200 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(; and base temperature is \)40^{\circ} \mathrm{C}$. The heat transfer coefficient is \(20 \mathrm{~W} / \mathrm{m}^{2}\). . Estimate the fin temperature at a distance of \(5.0 \mathrm{~cm}\) from the base and the rate of heat loss from the entire fin.

A spherical vessel, \(3.0 \mathrm{~m}\) in diameter (and negligible wall thickness), is used for storing a fluid at a temperature of $0^{\circ} \mathrm{C}\(. The vessel is covered with a \)5.0$-cm-thick layer of an insulation \((k=0.20 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\). The surrounding air is at \(22^{\circ} \mathrm{C}\). The inside and outside heat transfer coefficients are 40 and 10 $\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}\(, respectively. Calculate \)(a)$ all thermal resistances, in \(\mathrm{K} / \mathrm{W},(b)\) the steady rate of heat transfer, and \((c)\) the temperature difference across the insulation layer.

Consider a \(1.5\)-m-high electric hot-water heater that has a diameter of $40 \mathrm{~cm}\( and maintains the hot water at \)60^{\circ} \mathrm{C}$. The tank is located in a small room whose average temperature is $27^{\circ} \mathrm{C}$, and the heat transfer coefficients on the inner and outer surfaces of the heater are 50 and $12 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, respectively. The tank is placed in another \(46-\mathrm{cm}\)-diameter sheet metal tank of negligible thickness, and the space between the two tanks is filled with foam insulation $(k=0.03 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$. The thermal resistances of the water tank and the outer thin sheet metal shell are very small and can be neglected. The price of electricity is \(\$ 0.08 / \mathrm{kWh}\), and the homeowner pays \(\$ 280\) a year for water heating. Determine the fraction of the hot-water energy cost of this household that is due to the heat loss from the tank. Hot-water tank insulation kits consisting of 3 -cm-thick fiberglass insulation \((k=0.035 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) large enough to wrap the entire tank are available in the market for about \(\$ 30\). If such an insulation is installed on this water tank by the homeowner himself, how long will it take for this additional insulation to pay for itself?

An ASTM B209 5154 aluminum alloy plate is connected to an insulation plate by long metal bolts \(4.8 \mathrm{~mm}\) in diameter. The portion of the bolts exposed to convection heat transfer with air is \(5 \mathrm{~cm}\) long. The thermal conductivity of the bolt is known to be $15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(. The ambient condition of the air is at \)20^{\circ} \mathrm{C}\( with a convection heat transfer coefficient of \)20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. According to the ASME Code for Process Piping (ASME B31.3-2014, Table A-1M), the maximum use temperature for the ASTM B209 5154 aluminum alloy plate is \(65^{\circ} \mathrm{C}\). If the temperature of the bolt at midlength ( \(2.5 \mathrm{~cm}\) from the upper surface of the aluminum plate) is \(50^{\circ} \mathrm{C}\), determine the temperature \(T_{b}\) at the upper surface of the aluminum plate. What is the rate of heat loss from each bolt to convection? Is the use of the ASTM B209 5154 plate in compliance with the ASME Code for Process Piping?

Consider two walls, \(A\) and \(B\), with the same surface areas and the same temperature drops across their thicknesses. The ratio of thermal conductivities is \(k_{A} / k_{B}=4\) and the ratio of the wall thicknesses is \(L_{A} / L_{B}=2\). The ratio of heat transfer rates through the walls \(\dot{Q}_{A} / \dot{Q}_{B}\) is (a) \(0.5\) (b) 1 (c) 2 (d) 4 (e) 8

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