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Consider a \(1.2\)-m-high and 2-m-wide doublepane window consisting of two \(3-\mathrm{mm}\)-thick layers of glass $(k=0.78 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\( separated by a \)2.5$-cm-wide airspace. Determine the steady rate of heat transfer through this window and the temperature of its inner surface for a day during which the room is maintained at \(20^{\circ} \mathrm{C}\) while the temperature of the outdoors is \(0^{\circ} \mathrm{C}\). Take the heat transfer coefficients on the inner and outer surfaces of the window to be \(h_{1}=10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and $h_{2}=25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, and disregard any heat transfer by radiation. Evaluate air properties at a film temperature of \(10^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\) pressure. Is this a good assumption?

Short Answer

Expert verified
Answer: The steady rate of heat transfer through the double-pane window is 444.4 W, and the temperature of its inner surface is 19.29°C. As the temperatures involved in this problem are relatively low, it is reasonable to assume that radiation has a minor effect compared to conduction and convection in this case.

Step by step solution

01

Calculate the resistances

First, we will compute the thermal resistance for each layer: the two layers of glass and the layer of air in between. For the glass layers, we have: $$R_{G} = \frac{\Delta x}{kA}$$ Where \(R_{G}\) is the thermal resistance of the glass, \(\Delta x = 3 \times 10^{-3}\,\text{m}\) is the thickness, \(k = 0.78 \frac{\mathrm{W}}{\mathrm{m}\cdot\mathrm{K}}\) is the thermal conductivity, and A is the area. Considering the dimensions of the window, the area is: $$A = 1.2\,\text{m} \times 2\,\text{m} = 2.4\,\mathrm{m^2}$$ Computing the resistance for the glass layers, we have: $$R_{G} = \frac{3 \times 10^{-3}\,\text{m}}{0.78 \frac{\mathrm{W}}{\mathrm{m}\cdot\mathrm{K}} \times 2.4\,\mathrm{m^2}} = 1.6026 \times 10^{-3}\,\mathrm{K/W}$$ Considering the air layer, the resistance is given by: $$R_{A} = \frac{1}{hA}$$ Where \(h = 10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) is the heat transfer coefficient and A is the area. Calculating the resistance, we have: $$R_{A} = \frac{1}{10 \frac{\mathrm{W}}{\mathrm{m}^{2}\cdot\mathrm{K}} \times 2.4\, \mathrm{m^2}} = 0.0417\,\mathrm{K/W}$$
02

Calculate the overall resistance and steady state heat transfer rate

Next, we will find the overall resistance by adding resistance of two glass layers and the air layer: $$R_{total} = 2R_{G} + R_{A}$$ $$R_{total} = 2(1.6026 \times 10^{-3}\,\mathrm{K/W}) + 0.0417 \,\mathrm{K/W} = 0.045\,\mathrm{K/W}$$ Now, we will compute the steady state heat transfer rate using the overall resistance and the given temperature difference: $$q = \frac{T_{1} - T_{2}}{R_{total}}$$ Where \(T_{1} = 20^{\circ} \mathrm{C}\) is the room temperature, \(T_{2} = 0^{\circ} \mathrm{C}\) is the outside temperature. Calculating the heat transfer rate, we have: $$q = \frac{20\,\mathrm{C} - 0\,\mathrm{C}}{0.045\, \mathrm{K/W}} = 444.4\,\mathrm{W}$$
03

Calculate the inner surface temperature

Finally, we will compute the temperature of the inner surface of the window. We will use the heat transfer rate and the resistance of the glass for this calculation: $$T_{surface} = T_{1} - q \times R_{G}$$ $$T_{surface} = 20^{\circ} \mathrm{C} - 444.4\,\mathrm{W} \times 1.6026 \times 10^{-3}\,\mathrm{K/W} = 19.29^{\circ} \mathrm{C}$$ Thus, the steady rate of heat transfer through the double-pane window is \(444.4\,\mathrm{W}\), and the temperature of its inner surface is \(19.29^{\circ} \mathrm{C}\). Regarding the assumption about disregarding radiation, since the temperatures involved in this problem are relatively low, it is reasonable to assume that radiation has a minor effect comparing to conduction and convection in this case.

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Most popular questions from this chapter

A horizontal \(1.5\)-m-wide, \(4.5\)-m-long double-pane window consists of two sheets of glass separated by a \(3.5-\mathrm{cm}\) gap filled with water. If the glass surface temperatures at the bottom and the top are measured to be \(60^{\circ} \mathrm{C}\) and \(40^{\circ} \mathrm{C}\), respectively, the rate of heat transfer through the window is (a) \(27.6 \mathrm{~kW}\) (b) \(39.4 \mathrm{~kW}\) (c) \(59.6 \mathrm{~kW}\) (d) \(66.4 \mathrm{~kW}\) (e) \(75.5 \mathrm{~kW}\) (For water, use $k=0.644 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \quad \operatorname{Pr}=3.55\(, \)\nu=0.554 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}, \beta=0.451 \times 10^{-3} \mathrm{~K}^{-1}$. Also, the applicable correlation is \(\mathrm{Nu}=0.069 \mathrm{Ra}^{1 / 3} \mathrm{Pr}^{0.074}\).)

Consider a \(2-\mathrm{m}\)-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 at \(20^{\circ} \mathrm{C}\) whose walls and ceiling are at about the same temperature. The tank is placed in a 44 -cm- diameter sheet metal shell of negligible thickness, and the space between the tank and the shell is filled with foam insulation. The average temperature and emissivity of the outer surface of the shell are \(40^{\circ} \mathrm{C}\) and \(0.7\), respectively. The price of electricity is \(\$ 0.08 / \mathrm{kWh}\). Hot-water tank insulation kits large enough to wrap the entire tank are available on the market for about \(\$ 60\). If such an insulation kit is installed on this water tank by the homeowner himself, how long will it take for this additional insulation to pay for itself? Disregard any heat loss from the top and bottom surfaces, and assume the insulation reduces the heat losses by 80 percent.

A solar collector consists of a horizontal copper tube of outer diameter $5 \mathrm{~cm}\( enclosed in a concentric thin glass tube of \)9 \mathrm{~cm}$ diameter. Water is heated as it flows through the tube, and the annular space between the copper and glass tube is filled with air at \(1 \mathrm{~atm}\) pressure. During a clear day, the temperatures of the tube surface and the glass cover are measured to be \(60^{\circ} \mathrm{C}\) and $32^{\circ} \mathrm{C}$, respectively. Determine the rate of heat loss from the collector by natural convection per meter length of the tube. A?swer: \(17.4 \mathrm{~W}\)

A boiler supplies hot water to equipment through a horizontal pipe. The hot water exits the pipe and enters the equipment at \(98^{\circ} \mathrm{C}\). The outer diameter of the pipe is \(20 \mathrm{~mm}\), and the pipe distance between the boiler and the equipment is \(30 \mathrm{~m}\). The section of the pipe between the boiler and the equipment is exposed to natural convection with air at an ambient temperature of \(20^{\circ} \mathrm{C}\). The hot water flows steadily in the pipe at \(10 \mathrm{~g} / \mathrm{s}\), and its specific heat is \(4.2 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\). The temperature at the pipe surface is \(80^{\circ} \mathrm{C}\), and the pipe has an emissivity of \(0.6\) that contributes to the thermal radiation with the surroundings at \(20^{\circ} \mathrm{C}\). According to the service restrictions of the ASME Boiler and Pressure Vessel Code (ASME BPVC.IV-2015, HG-101), hot water boilers should not be operating at temperatures exceeding \(120^{\circ} \mathrm{C}\) at or near the boiler outlet. Determine whether the water temperature exiting the boiler is in compliance with the ASME Boiler and Pressure Vessel Code.

Two concentric spheres with diameters of \(5 \mathrm{~cm}\) and $10 \mathrm{~cm}\( have their surface temperatures maintained at \)100^{\circ} \mathrm{C}\( and \)200^{\circ} \mathrm{C}$, respectively. The enclosure between the two concentric spherical surfaces is filled with nitrogen gas at \(\mathrm{atm}\). Determine the rate of heat transfer through the enclosure.

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