Consider a house that is maintained at a constant temperature of \(22^{\circ} \mathrm{C}\). One of the walls of the house has three singlepane glass windows that are \(1.5 \mathrm{~m}\) high and \(1.8 \mathrm{~m}\) long. The glass \((k=0.78 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) is \(0.5 \mathrm{~cm}\) thick, and the heat transfer coefficient on the inner surface of the glass is \(8 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Now winds at \(35 \mathrm{~km} / \mathrm{h}\) start to blow parallel to the surface of this wall. If the air temperature outside is \(-2^{\circ} \mathrm{C}\), determine the rate of heat loss through the windows of this wall. Assume radiation heat transfer to be negligible. Evaluate the air properties at a film temperature of \(5^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\).

Short Answer

Expert verified
#Answer# Based on the given information and calculations, the rate of heat loss through the windows is: $$ Q = \frac{24^{\circ}\mathrm{C}}{R_{total}} $$ Where $R_{total}$ is the combined thermal resistance found in Step 2. By plugging in the values and calculating, we can determine the rate of heat loss through the windows.

Step by step solution

01

Calculate the Area of the Windows

First, we will calculate the area of each window, which will be used later in our calculations. The dimensions given are 1.5 m high and 1.8 m long, so the area of one window is: $$ A = (1.5\,\mathrm{m})(1.8\,\mathrm{m}) = 2.7\,\mathrm{m}^2 $$ There are three windows, so the total area of the windows is: $$ A_{total} = 3 \times A = 3 \times 2.7\,\mathrm{m}^2 = 8.1\,\mathrm{m}^2 $$
02

Calculate Thermal Resistance of Glass and Convective Heat Transfer Coefficients

Now that we have the area of the windows, we will calculate the combined thermal resistance of conduction through the glass and convection at the inner surface of the glass. First, the thermal resistance of conduction through the glass can be expressed as: $$ R_{cond} = \frac{L}{kA} = \frac{0.005\,\mathrm{m}}{0.78\,\mathrm{W/m\,K}\times 8.1\,\mathrm{m}^2} $$ Next, compute the thermal resistance of convection at the inner surface of the glass: $$ R_{conv} = \frac{1}{hA} = \frac{1}{8\,\mathrm{W/m^2\,K} \times 8.1\,\mathrm{m}^2} $$ Then, find the total combined thermal resistance by adding these two values: $$ R_{total} = R_{cond} + R_{conv} $$
03

Calculate Temperature Difference

The temperature difference between the inside and outside of the house is needed to find the rate of heat loss. The inside temperature is 22°C, and the outside temperature is -2°C. The temperature difference is: $$ \Delta T = T_{inside} - T_{outside} = 22^{\circ}\mathrm{C} - (-2^{\circ}\mathrm{C}) = 24^{\circ}\mathrm{C} $$
04

Calculate Rate of Heat Loss

Now that we have the combined thermal resistance and temperature difference, we can determine the rate of heat loss through the windows using the following equation: $$ Q = \frac{\Delta T}{R_{total}} $$ Plug in the values calculated in previous steps and find the rate of heat loss through the windows.

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Most popular questions from this chapter

Air at \(20^{\circ} \mathrm{C}(1 \mathrm{~atm})\) is flowing over a \(5-\mathrm{cm}\) diameter sphere with a velocity of \(3.5 \mathrm{~m} / \mathrm{s}\). If the surface temperature of the sphere is constant at \(80^{\circ} \mathrm{C}\), determine \((a)\) the average drag coefficient on the sphere and \((b)\) the heat transfer rate from the sphere.

Air \((k=0.028 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=0.7)\) at \(50^{\circ} \mathrm{C}\) flows along a 1 -m-long flat plate whose temperature is maintained at \(20^{\circ} \mathrm{C}\) with a velocity such that the Reynolds number at the end of the plate is 10,000 . The heat transfer per unit width between the plate and air is (a) \(20 \mathrm{~W} / \mathrm{m}\) (b) \(30 \mathrm{~W} / \mathrm{m}\) (c) \(40 \mathrm{~W} / \mathrm{m}\) (d) \(50 \mathrm{~W} / \mathrm{m}\) (e) \(60 \mathrm{~W} / \mathrm{m}\)

In flow over cylinders, why does the drag coefficient suddenly drop when the flow becomes turbulent? Isn't turbulence supposed to increase the drag coefficient instead of decreasing it?

What is drag? What causes it? Why do we usually try to minimize it?

Air at \(25^{\circ} \mathrm{C}\) flows over a 5 -cm-diameter, 1.7-m-long smooth pipe with a velocity of \(4 \mathrm{~m} / \mathrm{s}\). A refrigerant at \(-15^{\circ} \mathrm{C}\) flows inside the pipe and the surface temperature of the pipe is essentially the same as the refrigerant temperature inside. The drag force exerted on the pipe by the air is (a) \(0.4 \mathrm{~N}\) (b) \(1.1 \mathrm{~N}\) (c) \(8.5 \mathrm{~N}\) (d) \(13 \mathrm{~N}\) (e) \(18 \mathrm{~N}\) (For air, use \(\nu=1.382 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}, \rho=1.269 \mathrm{~kg} / \mathrm{m}^{3}\) )

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