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The inner and outer glasses of a 4-ft \(\times 4\)-ft double-pane window are at \(60^{\circ} \mathrm{F}\) and \(48^{\circ} \mathrm{F}\), respectively. If the \(0.25\)-in space between the two glasses is filled with still air, determine the rate of heat transfer through the window. Answer. $131 \mathrm{Btu} / \mathrm{h}$

Short Answer

Expert verified
Answer: The rate of heat transfer through the double-pane window is 131 Btu/h.

Step by step solution

01

Identify the relevant parameters

We are given the following information: - Dimensions of window: 4 ft x 4 ft - Inner glass temperature: \(T_1 = 60^\circ\text{F}\) - Outer glass temperature: \(T_2 = 48^\circ\text{F}\) - Air space thickness: \(d = 0.25\text{ in}\) To determine the rate of heat transfer, we also need the thermal conductivity of air, which is approximately \(k_{air} = 0.015 \text{Btu}/(\text{h}\cdot\text{ft}\cdot\text{F})\).
02

Calculate the thermal resistance due to the air space

As the heat flows perpendicularly through the window, we can consider a 1-dimensional heat transfer. The thermal resistance of the air space can be calculated using the equation for conduction resistance, which is: $$R_{air} = \frac{d}{k A}$$ First, we need to convert \(d\) from inches to feet: \(d = 0.25 \text{ in} \cdot \frac{1\text{ ft}}{12\text{ in}} = \frac{1}{48} \text{ ft}\). Next, we calculate the area of the window, \(A = 4 \text{ft}\times 4 \text{ft} = 16 \text{ft}^2\). Now, we can find the thermal resistance: $$R_{air} = \frac{\frac{1}{48} \text{ft}}{0.015 \frac{\text{Btu}}{\text{h}\cdot\text{ft}\cdot\text{F}}\cdot 16 \text{ft}^2} = 0.18056\, \text{h}\cdot\text{F}/\text{Btu}$$
03

Calculate the rate of heat transfer

To find the rate of heat transfer \(q\), we can use the equation for heat transfer through a composite wall: $$q=\frac{\Delta T}{R_{total}}$$ Since we only have one layer of resistance (the air space), the total resistance is \(R_{total} = R_{air}\). The temperature difference across the window is \(\Delta T = T_1 - T_2 = 60^\circ\text{F} - 48^\circ\text{F} = 12^\circ\text{F}\). Substituting values, we get: $$q = \frac{12 \text{F}}{0.18056\,\text{h}\cdot\text{F}/\text{Btu}} = 131.00\, \text{Btu/h}$$ The rate of heat transfer through the window is \(131 \text{Btu/h}\).

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Most popular questions from this chapter

A person standing in a room loses heat to the air in the room by convection and to the surrounding surfaces by radiation. Both the air in the room and the surrounding surfaces are at \(20^{\circ} \mathrm{C}\). The exposed surface of the person is \(1.5 \mathrm{~m}^{2}\) and has an average temperature of \(32^{\circ} \mathrm{C}\) and an emissivity of \(0.90\). If the rates of heat transfer from the person by convection and by radiation are equal, the combined heat transfer coefficient is (a) \(0.008 \mathrm{~W} / \mathrm{m}^{2}, \mathrm{~K}\) (b) \(3.0 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (c) \(5.5 \mathrm{~W} / \mathrm{m}^{2}, \mathrm{~K}\) (d) \(8.3 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (e) \(10.9 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\)

A 30 -cm-diameter black ball at \(120^{\circ} \mathrm{C}\) is suspended in air. It is losing heat to the surrounding air at \(25^{\circ} \mathrm{C}\) by convection with a heat transfer coefficient of $12 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$ and by radiation to the surrounding surfaces at \(15^{\circ} \mathrm{C}\). The total rate of heat transfer from the black ball is (a) \(322 \mathrm{~W}\) (b) \(595 \mathrm{~W}\) (c) \(234 \mathrm{~W}\) (d) \(472 \mathrm{~W}\) (e) \(2100 \mathrm{~W}\)

Consider steady heat transfer between two large parallel plates at constant temperatures of \(T_{1}=290 \mathrm{~K}\) and \(T_{2}=150 \mathrm{~K}\) that are \(L=2 \mathrm{~cm}\) apart. Assuming the surfaces to be black (emissivity \(\varepsilon=1\) ), determine the rate of heat transfer between the plates per unit surface area assuming the gap between the plates is \((a)\) filled with atmospheric air, \((b)\) evacuated, \((c)\) filled with fiberglass insulation, and \((d)\) filled with superinsulation having an apparent thermal conductivity of \(0.00015 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\).

In a power plant, pipes transporting superheated vapor are very common. Superheated vapor is flowing at a rate of \(0.3 \mathrm{~kg} / \mathrm{s}\) inside a pipe \(5 \mathrm{~cm}\) in diameter and \(10 \mathrm{~m}\) in length. The pipe is located in a power plant at \(20^{\circ} \mathrm{C}\) and has a uniform surface temperature of \(100^{\circ} \mathrm{C}\). If the temperature drop between the inlet and exit of the pipe is \(30^{\circ} \mathrm{C}\), and the specific heat of the vapor is $2190 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$, determine the heat transfer coefficient as a result of convection between the pipe surface and the surroundings.

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