Determine the \(U\)-factor for the center-of-glass section of a double-pane window with a 13-mm air space for winter design conditions. The glazings are made of clear glass having an emissivity of \(0.84\). Take the average air space temperature at design conditions to be \(10^{\circ} \mathrm{C}\) and the temperature difference across the air space to be \(15^{\circ} \mathrm{C}\).

Short Answer

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Answer: The U-factor for the center-of-glass section of a double-pane window with a 13-mm air space for winter design conditions is approximately 512.48 W/(m²·K).

Step by step solution

01

Calculate heat transfer coefficient due to conduction through the glass

We will first calculate the resistance for conduction through the glass, which can be determined by the equation: \(R_\text{cond}=\frac{d}{kA}\), where \(d\) is the thickness of the glass, \(k\) is the thermal conductivity of the glass, and \(A\) is the area of the glass. We know the thermal conductivity of glass to be \(k=1 \,\text{W}\,(\text{m} \cdot \text{K})^{-1}\). Assuming the glass thickness to be \(4 \,\text{mm}\) and considering unit area \(A=1 \,\text{m}^{2}\), we have: \(R_\text{cond}=\frac{0.004\,\text{m}}{1\,\text{W}\,(\text{m} \cdot \text{K})^{-1} \cdot 1\,\text{m}^{2}}=0.004\,\text{m}^{2}\,(\text{K}\,\text{W})^{-1}\). The heat transfer coefficient for conduction through glass can be calculated as: \(U_\text{cond}=\frac{1}{R_\text{cond}}=\frac{1}{0.004\,\text{m}^{2}\,(\text{K}\,\text{W})^{-1}}=250\,\text{W}\,(\text{m}^{2}\cdot\text{K})^{-1}\).
02

Calculate the heat transfer coefficient due to radiation in the air space

We will now calculate the radiation heat transfer coefficient (\(U_\text{rad}\)) within the air space using the following equation: \(U_\text{rad}=\frac{\sigma\epsilon(Th^{4}-Tc^{4})}{Th-Tc}\), where \(\sigma\) is the Stefan-Boltzmann constant (\(5.67\times10^{-8}\,\text{W}\,(\text{m}^{2}\cdot\text{K}^{4})^{-1}\)), \(\epsilon\) is the emissivity of the glass, \(Th\) is the hot surface temperature and \(Tc\) is the cold surface temperature. We are given the emissivity of the glass as \(0.84\), the average air space temperature as \(10^{\circ}\mathrm{C}\), and the temperature difference across the air space as \(15^{\circ}\mathrm{C}\). First, determine the hot and cold surface temperatures: \(Th=10+7.5=17.5^{\circ}\mathrm{C}=290.65\,\text{K}\), \(Tc=10-7.5=2.5^{\circ}\mathrm{C}=275.65\,\text{K}\). Now, calculate the radiation heat transfer coefficient: \(U_\text{rad}=\frac{5.67\times10^{-8}\,\text{W}\,(\text{m}^{2}\cdot\text{K}^{4})^{-1} \cdot 0.84 \cdot (290.65^{4}-275.65^{4})}{290.65-275.65} \approx 8.12\,\text{W}\,(\text{m}^{2}\cdot\text{K})^{-1}\).
03

Calculate the heat transfer coefficient due to convection in the air space

We will now calculate the convection heat transfer coefficient (\(U_\text{conv}\)) within the air space using the following equation: \(U_\text{conv}=1.32\Delta T^{1/3}\), where \(\Delta T\) is the temperature difference across the air space. Given the temperature difference across the air space as \(15^{\circ}\mathrm{C}\), we have: \(U_\text{conv}=1.32\cdot15^{1/3}\approx 4.36\,\text{W}\,(\text{m}^{2}\cdot\text{K})^{-1}\).
04

Calculate the overall U-factor

Finally, we will calculate the overall U-factor by summing up the heat transfer coefficients from the above steps. Since the window has two glass panes, we need to consider the conduction through both panes. Therefore, \(U_\text{total}=U_\text{cond}+U_\text{rad}+U_\text{conv}+U_\text{cond} = 250 + 8.12 + 4.36 + 250 \approx 512.48\,\text{W}\,(\text{m}^{2}\cdot\text{K})^{-1}\). The U-factor for the center-of-glass section of a double-pane window with a 13-mm air space for winter design conditions is approximately \(512.48\,\text{W}\,(\text{m}^{2}\cdot\text{K})^{-1}\).

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Most popular questions from this chapter

Skylights or "roof windows" are commonly used in homes and manufacturing facilities since they let natural light in during day time and thus reduce the lighting costs. However, they offer little resistance to heat transfer, and large amounts of energy are lost through them in winter unless they are equipped with a motorized insulating cover that can be used in cold weather and at nights to reduce heat losses. Consider a 1 -m-wide and \(2.5\)-m-long horizontal skylight on the roof of a house that is kept at \(20^{\circ} \mathrm{C}\). The glazing of the skylight is made of a single layer of \(0.5\)-cm-thick glass \((k=0.78 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and \(\varepsilon=0.9)\). Determine the rate of heat loss through the skylight when the air temperature outside is \(-10^{\circ} \mathrm{C}\) and the effective sky temperature is \(-30^{\circ} \mathrm{C}\). Compare your result with the rate of heat loss through an equivalent surface area of the roof that has a common \(R-5.34\) construction in SI units (i.e., a thickness-to-effective-thermal- conductivity ratio of \(\left.5.34 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\right)\). Evaluate air properties at a film temperature of \(-7^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\) pressure. Is this a good assumption?

During a visit to a plastic sheeting plant, it was observed that a 60 -m-long section of a 2 -in nominal \((6.03\)-cm-outerdiameter) steam pipe extended from one end of the plant to the other with no insulation on it. The temperature measurements at several locations revealed that the average temperature of the exposed surfaces of the steam pipe was \(170^{\circ} \mathrm{C}\), while the temperature of the surrounding air was \(20^{\circ} \mathrm{C}\). The outer surface of the pipe appeared to be oxidized, and its emissivity can be taken to be \(0.7\). Taking the temperature of the surrounding surfaces to be \(20^{\circ} \mathrm{C}\) also, determine the rate of heat loss from the steam pipe. Steam is generated in a gas furnace that has an efficiency of 78 percent, and the plant pays \(\$ 1.10\) per therm ( 1 therm \(=\) \(105,500 \mathrm{~kJ}\) ) of natural gas. The plant operates \(24 \mathrm{~h}\) a day 365 days a year, and thus \(8760 \mathrm{~h}\) a year. Determine the annual cost of the heat losses from the steam pipe for this facility.

A 4-m-diameter spherical tank contains iced water at \(0^{\circ} \mathrm{C}\). The tank is thin-shelled and thus its outer surface temperature may be assumed to be same as the temperature of the iced water inside. Now the tank is placed in a large lake at \(20^{\circ} \mathrm{C}\). The rate at which the ice melts is (a) \(0.42 \mathrm{~kg} / \mathrm{s}\) (b) \(0.58 \mathrm{~kg} / \mathrm{s}\) (c) \(0.70 \mathrm{~kg} / \mathrm{s}\) (d) \(0.83 \mathrm{~kg} / \mathrm{s}\) (e) \(0.98 \mathrm{~kg} / \mathrm{s}\) (For lake water, use \(k=0.580 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=9.45, v=\) \(0.1307 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}, \beta=0.138 \times 10^{-3} \mathrm{~K}^{-1}\) )

Will a hot horizontal plate whose back side is insulated cool faster or slower when its hot surface is facing down instead of up?

A hot fluid \(\left(k_{\text {fluid }}=0.72 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right)\) is flowing as a laminar fully-developed flow inside a pipe with an inner diameter of \(35 \mathrm{~mm}\) and a wall thickness of \(5 \mathrm{~mm}\). The pipe is \(10 \mathrm{~m}\) long and the outer surface is exposed to air at \(10^{\circ} \mathrm{C}\). The average temperature difference between the hot fluid and the pipe inner surface is \(\Delta T_{\text {avg }}=10^{\circ} \mathrm{C}\), and the inner and outer surface temperatures are constant. Determine the outer surface temperature of the pipe. Evaluate the air properties at \(50^{\circ} \mathrm{C}\). Is this a good assumption?

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