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Consider a \(1.5\)-m-high and 2.4-m-wide doublepane window consisting of two \(3-\mathrm{mm}\)-thick layers of glass $(k=0.78 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\( separated by a \)12-\mathrm{mm}\(-wide stagnant airspace \)(k=0.026 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$. Determine the steady rate of heat transfer through this double-pane window and the temperature of its inner surface for a day during which the room is maintained at $21^{\circ} \mathrm{C}\( while the temperature of the outdoors is \)-5^{\circ} \mathrm{C}$. Take the convection 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.

Short Answer

Expert verified
Answer: The steady rate of heat transfer through the double-pane window is 374.64 W, and the temperature of the inner surface is 10.59 °C.

Step by step solution

01

Calculate the area of the window

First, we need to calculate the area of the window. It is given that the window has a height of 1.5 m and a width of 2.4 m. Area = Height × Width = 1.5 m × 2.4 m = 3.6 m^2
02

Calculate the thermal resistances

Next, we can find the thermal resistances for each layer of the window. For the glass panes, it is given that they have a thickness of 3 mm and a thermal conductivity of 0.78 W/m·K. For the air space, the thickness is 12 mm, and the thermal conductivity is 0.026 W/m·K. We also have the convection heat transfer coefficients for the inner and outer surfaces, h1 = 10 W/m^2·K, and h2 = 25 W/m^2·K. Using these parameters, we can find the thermal resistances as follows: R1 (convection) = 1 / (h1 × Area) = 1 / (10 W/m^2·K × 3.6 m^2) = 0.0278 m^2·K/W R2 (glass) = Thickness / (k × Area) = 0.003 m / (0.78 W/m·K × 3.6 m^2) = 0.00137 m^2·K/W R3 (air space) = 0.012 m / (0.026 W/m·K × 3.6 m^2) = 0.0377 m^2·K/W R4 (glass) = 0.003 m / (0.78 W/m·K × 3.6 m^2) = 0.00137 m^2·K/W R5 (convection) = 1 / (h2 × Area) = 1 / (25 W/m^2·K × 3.6 m^2) = 0.00111 m^2·K/W
03

Calculate the total thermal resistance

Now we can calculate the total thermal resistance of the system by summing up the individual resistances: R_total = R1 + R2 + R3 + R4 + R5 = 0.0278 + 0.00137 + 0.0377 + 0.00137 + 0.00111 = 0.0694 m^2·K/W
04

Calculate the steady rate of heat transfer

We can calculate the steady rate of heat transfer through the double-pane window using the overall resistance and the temperature difference between the indoor and outdoor environments: Q = ΔT / R_total = (21 - (-5)) °C / 0.0694 m^2·K/W = 26 K / 0.0694 m^2·K/W = 374.64 W
05

Calculate the temperature of the inner surface

Now we can find the temperature of the inner surface using the heat transfer rate and the convection resistance at the inner surface: ΔT1 = Q × R1 = 374.64 W × 0.0278 m^2·K/W = 10.41 K The temperature of the inner surface is then: T_inner = T_room - ΔT1 = 21 °C - 10.41 K = 10.59 °C
06

Final Results

The steady rate of heat transfer through the double-pane window is 374.64 W, and the temperature of the inner surface is 10.59 °C.

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Most popular questions from this chapter

The overall heat transfer coefficient (the \(U\)-value) of a wall under winter design conditions is \(U=1.40 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Determine the \(U\)-value of the wall under summer design conditions.

A 12 -m-long and 8-cm-diameter hot-water pipe of a district heating system is buried in the soil \(80 \mathrm{~cm}\) below the ground surface. The outer surface temperature of the pipe is \(60^{\circ} \mathrm{C}\). Taking the surface temperature of the earth to be \(2^{\circ} \mathrm{C}\) and the thermal conductivity of the soil at that location to be $0.9 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$, determine the rate of heat loss from the pipe.

A cylindrical resistor element on a circuit board dissipates $0.15 \mathrm{~W}\( of power in an environment at \)40^{\circ} \mathrm{C}$. The resistor is \(1.2 \mathrm{~cm}\) long, and has a diameter of \(0.3 \mathrm{~cm}\). Assuming heat to be transferred uniformly from all surfaces, determine \((a)\) the amount of heat this resistor dissipates during a 24 -h period; (b) the heat flux on the surface of the resistor, in $\mathrm{W} / \mathrm{m}^{2}$; and (c) the surface temperature of the resistor for a combined convection and radiation heat transfer coefficient of $9 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$.

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?

A pipe is insulated such that the outer radius of the insulation is less than the critical radius. Now the insulation is taken off. Will the rate of heat transfer from the pipe increase or decrease for the same pipe surface temperature?

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