Consider a \(1.2\)-m-high and 2-m-wide double-pane window consisting of two 3-mm-thick layers of glass \((k=\) \(0.78 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) separated by a \(3-\mathrm{cm}\)-wide air space. 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
The steady heat transfer through the double-pane window without considering the air layer convective resistance is 327.9 W, and the temperature of the inner surface is 18.64°C. Including the air layer convective resistance, which was not given, would potentially change the results slightly.

Step by step solution

01

Find the total thermal resistance of the system

To find the total thermal resistance, we will consider all the thermal resistances in series: 1. Convection resistance from the room to the inner glass surface 2. Conduction resistance through the first glass layer 3. Convective resistance from the first air layer to the second glass layer 4. Conduction resistance through the second glass layer 5. Convective resistance from the second glass layer to the outside The convection resistance is given by: $$R_{conv} = \frac{1}{hA}$$ The conduction resistance is given by: $$R_{cond} = \frac{L}{kA}$$ where: \(h\) = heat transfer coefficient \(A\) = surface area \(L\) = thickness of the conduction material \(k\) = thermal conductivity Calculating the given values, we have: Area of the window, \(A = 1.2 * 2 = 2.4 \ \mathrm{m^2}\) Thickness of glass, \(L_{glass} = 3 * 10^{-3} \ \mathrm{m}\) Width of air space, \(L_{air} = 3*10^{-2} \ \mathrm{m}\) Now let's calculate individual thermal resistances: 1. \(R_{conv1} = \frac{1}{(10)(2.4)} = 0.04167 \ \mathrm{m^2 K/W}\) 2. \(R_{cond1} = \frac{3*10^{-3}}{(0.78)(2.4)} = 0.001282 \ \mathrm{m^2 K/W}\) 3. \(R_{conv2}\) of air layer is missing. We will address this in the assumption evaluation part. 4. \(R_{cond2} = \frac{3*10^{-3}}{(0.78)(2.4)} = 0.001282 \ \mathrm{m^2 K/W}\) 5. \(R_{conv3} = \frac{1}{(25)(2.4)} = 0.01667 \ \mathrm{m^2 K/W}\) The total thermal resistance (excluding the air layer) is the sum of all individual resistances: $$R_{total} = R_{conv1} + R_{cond1} + R_{cond2} + R_{conv3} = 0.04167 + 0.001282 + 0.001282 + 0.01667 = 0.0609 \ \mathrm{m^2 K/W}$$ Now let's evaluate the assumption part and address the missing air layer.
02

Evaluate the assumption and find the missing air layer convection resistance

The problem asks if it's a good idea to disregard the heat transfer by radiation and evaluate air properties at a film temperature of \(10^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\) pressure. The heat transfer through the air layer is mainly by conduction, which is insignificant compared to conduction through the glass and convection, and therefore this assumption is reasonable. The air properties can also be evaluated at a film temperature of \(10^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\) pressure. Since radiation heat transfer is neglected, we only need to consider the convective heat transfer coefficient inside the air gap. However, we don't have this value in the given information. Hence, this step remains incomplete.
03

Find the steady rate of heat transfer

We know the total thermal resistance calculated earlier (excluding the air layer) and the temperature difference between the room and outside. Now we can find the steady heat transfer rate using the formula: $$Q = \frac{T_{room} - T_{outside}}{R_{total}}$$ Substitute the given values: $$Q = \frac{20 - 0}{0.0609} = 327.9 \ \mathrm{W}$$
04

Find the temperature of the inner surface

Using the convective heat transfer equation: $$Q = h_{1}A(T_{room} - T_{surface1})$$ Rearranging the equation and solving for \(T_{surface1}\): $$T_{surface1} = T_{room} - \frac{Q}{h_{1}A} = 20 - \frac{327.9}{(10)(2.4)} = 18.64^{\circ} \mathrm{C}$$ The steady heat transfer through the double-pane window is \(327.9 \ \mathrm{W}\), and the temperature of the inner surface is \(18.64^{\circ} \mathrm{C}\). However, this solution doesn't consider the air layer convective resistance, which would possibly alter the results slightly.

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Thermal Resistance
Understanding thermal resistance is crucial in analyzing heat transfer through materials such as the glass in a double-pane window. Much like electrical resistance in the flow of electric current, thermal resistance quantifies how materials impede heat flow. In essence, it's a measure of a material’s ability to resist heat transfer. The total thermal resistance in a system is determined by summing the individual resistances of different layers and interfaces.

For a double-pane window, thermal resistance comes from convection at the glass surfaces and conduction through the glass panes and the air gap. Mathematically, we represent the convection resistance as \( R_{conv} = \frac{1}{hA} \) and conduction resistance as \( R_{cond} = \frac{L}{kA} \) where \( h \) is the heat transfer coefficient, \( A \) is the surface area, \( L \) is the thickness of the material, and \( k \) is the material's thermal conductivity.

For instance, the sum of the thermal resistances through each glass layer and the air gap in a double-pane window helps us predict the efficiency of the window in insulating a room against cold outside temperatures.
Convection Heat Transfer
Convection heat transfer plays a significant role in the efficiency of a double-pane window. It involves the transfer of heat between a solid surface and the adjacent liquid or gas in motion. In the context of a window, convection occurs at both the inner and outer surfaces of the glass panes.

When considering double-pane windows, we take into account the heat transfer coefficient (\( h \)), which represents how well the material interacts with the surrounding environment to exchange heat. The higher the coefficient, the more efficient the heat transfer. In an ideal case, to maintain a consistent room temperature, you would want higher convection rates on the outside, removing heat from the window surface into the cooler outdoor air, and lower convection rates on the inside, to keep the indoor heat.
Conduction Heat Transfer
Conduction is the process through which heat is transferred directly through a material, moving from a higher temperature region to a lower temperature one. As the core component of a double-pane window, glass is a key material we consider for conduction. The thermal conductivity (\( k \)) of the glass indicates how well it conducts heat.

For our double-pane window scenario, we have two layers of glass and an air gap. The conduction resistance of each glass layer is given by \( R_{cond} = \frac{L}{kA} \) where \( L \) represents the thickness of the glass. The air gap also offers its own conduction resistance and can actually act as an insulator due to air's low thermal conductivity, further improving the window's efficiency. The amalgamation of these layers dictates the overall ability of the window to prevent heat loss.
Steady Heat Transfer Rate
The steady heat transfer rate is a consistent flow of thermal energy through a system over time. When we talk about the heat transfer rate through a window, we're referring to how much heat is lost from inside the home to the outside environment at a constant rate. In calculating this value for a double-pane window, we use \( Q = \frac{\Delta T}{R_{total}} \) where \( \Delta T \) is the temperature difference across the window and \( R_{total} \) is the total thermal resistance including convection and conduction components.

This consistent rate allows us to estimate energy loss so that heating systems can be designed or augmented to maintain the desired indoor temperature irrespective of external conditions. Energy-efficient windows, which minimize the steady heat transfer rate, are increasingly vital for reducing heating costs and conserving energy.
Temperature Distribution
In the context of a double-pane window, temperature distribution refers to how temperature varies across different points in the window system. The inner and outer surfaces of the window will have different temperatures due to loss of heat through the window layers, governed by the laws of heat conduction and convection.

An accurate understanding of temperature distribution is essential for determining the inner surface temperature of the glass, which affects not only the comfort levels within a room but also the window's overall thermal performance. Using principles of thermal resistance and the steady state assumption, we can calculate the temperature drop across each layer. The room's maintained temperature and the calculated heat transfer rate allow for the estimation of the inner surface temperature, providing us with a comprehensive view of the thermal behavior of the window system.

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Most popular questions from this chapter

In an ordinary double-pane window, about half of the heat transfer is by radiation. Describe a practical way of reducing the radiation component of heat transfer.

Exhaust gases from a manufacturing plant are being discharged through a \(10-\mathrm{m}-\) tall exhaust stack with outer diameter of \(1 \mathrm{~m}\). The exhaust gases are discharged at a rate of \(0.125 \mathrm{~kg} / \mathrm{s}\), while temperature drop between inlet and exit of the exhaust stack is \(30^{\circ} \mathrm{C}\), and the constant pressure-specific heat of the exhaust gases is \(1600 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\). On a particular calm day, the surrounding quiescent air temperature is \(33^{\circ} \mathrm{C}\). Solar radiation is incident on the exhaust stack outer surface at a rate of \(500 \mathrm{~W} / \mathrm{m}^{2}\), and both the emissivity and solar absorptivity of the outer surface are \(0.9\). Determine the exhaust stack outer surface temperature. Assume the film temperature is \(60^{\circ} \mathrm{C}\).

A vertical \(1.5\)-m-high and \(3.0\)-m-wide enclosure consists of two surfaces separated by a \(0.4-\mathrm{m}\) air gap at atmospheric pressure. If the surface temperatures across the air gap are measured to be \(280 \mathrm{~K}\) and \(336 \mathrm{~K}\) and the surface emissivities to be \(0.15\) and \(0.90\), determine the fraction of heat transferred through the enclosure by radiation. Answer: \(0.30\)

Consider a \(15-\mathrm{cm} \times 20\)-cm printed circuit board \((\mathrm{PCB})\) that has electronic components on one side. The board is placed in a room at \(20^{\circ} \mathrm{C}\). The heat loss from the back surface of the board is negligible. If the circuit board is dissipating \(8 \mathrm{~W}\) of power in steady operation, determine the average temperature of the hot surface of the board, assuming the board is \((a)\) vertical, \((b)\) horizontal with hot surface facing up, and (c) horizontal with hot surface facing down. Take the emissivity of the surface of the board to be \(0.8\) and assume the surrounding surfaces to be at the same temperature as the air in the room. Evaluate air properties at a film temperature of \(32.5^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\) pressure. Is this a good assumption?

An electric resistance space heater is designed such that it resembles a rectangular box \(50 \mathrm{~cm}\) high, \(80 \mathrm{~cm}\) long, and \(15 \mathrm{~cm}\) wide filled with \(45 \mathrm{~kg}\) of oil. The heater is to be placed against a wall, and thus heat transfer from its back surface is negligible. The surface temperature of the heater is not to exceed \(75^{\circ} \mathrm{C}\) in a room at \(25^{\circ} \mathrm{C}\) for safety considerations. Disregarding heat transfer from the bottom and top surfaces of the heater in anticipation that the top surface will be used as a shelf, determine the power rating of the heater in W. Take the emissivity of the outer surface of the heater to be \(0.8\) and the average temperature of the ceiling and wall surfaces to be the same as the room air temperature. Also, determine how long it will take for the heater to reach steady operation when it is first turned on (i.e., for the oil temperature to rise from \(25^{\circ} \mathrm{C}\) to \(75^{\circ} \mathrm{C}\) ). State your assumptions in the calculations.

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