Chapter 9: Problem 126
How do the relative magnitudes of \(U\)-factors of windows with aluminum, wood, and vinyl frames compare? Assume the windows are identical except for the frames.
Chapter 9: Problem 126
How do the relative magnitudes of \(U\)-factors of windows with aluminum, wood, and vinyl frames compare? Assume the windows are identical except for the frames.
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Get started for freeWhen neither natural nor forced convection is negligible, is it correct to calculate each independently and add them to determine the total convection heat transfer?
A solar collector consists of a horizontal aluminum tube of outer diameter $5 \mathrm{~cm}\( enclosed in a concentric thin glass tube of \)7 \mathrm{~cm}$ diameter. Water is heated as it flows through the aluminum tube, and the annular space between the aluminum and glass tubes is filled with air at $1 \mathrm{~atm}$ pressure. The pump circulating the water fails during a clear day, and the water temperature in the tube starts rising. The aluminum tube absorbs solar radiation at a rate of \(20 \mathrm{~W}\) per meter length, and the temperature of the ambient air outside is \(30^{\circ} \mathrm{C}\). Approximating the surfaces of the tube and the glass cover as being black (emissivity \(\varepsilon=1\) ) in radiation calculations and taking the effective sky temperature to be \(20^{\circ} \mathrm{C}\), determine the temperature of the aluminum tube when equilibrium is established (i.e., when the net heat loss from the tube by convection and radiation equals the amount of solar energy absorbed by the tube). For evaluation of air properties at $1 \mathrm{~atm}\( pressure, assume \)33^{\circ} \mathrm{C}$ for the surface temperature of the glass cover and \(45^{\circ} \mathrm{C}\) for the aluminum tube temperature. Are these good assumptions?
The side surfaces of a 3 -m-high cubic industrial furnace burning natural gas are not insulated, and the temperature at the outer surface of this section is measured to be \(110^{\circ} \mathrm{C}\). The temperature of the furnace room, including its surfaces, is \(30^{\circ} \mathrm{C}\), and the emissivity of the outer surface of the furnace is \(0.7\). It is proposed that this section of the furnace wall be insulated with glass wool insulation $(k=0.038 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$ wrapped by a reflective sheet \((\varepsilon=0.2)\) in order to reduce the heat loss by 90 percent. Assuming the outer surface temperature of the metal section still remains at about \(110^{\circ} \mathrm{C}\), determine the thickness of the insulation that needs to be used. The furnace operates continuously throughout the year and has an efficiency of 78 percent. The price of the natural gas is \(\$ 1.10 /\) therm ( 1 therm \(=105,500 \mathrm{~kJ}\) of energy content). If the installation of the insulation will cost \(\$ 550\) for materials and labor, determine how long it will take for the insulation to pay for itself from the energy it saves.
Skylights or "roof windows" are commonly used in homes and manufacturing facilities since they let natural light in during daytime 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 \(1-\mathrm{m}\)-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 \(0.5-\mathrm{cm}\)-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 $5.34 \mathrm{~m}^{2} . \mathrm{K} / \mathrm{W}\( ). Evaluate air properties at a film temperature of \)-7^{\circ} \mathrm{C}\( and \)1 \mathrm{~atm}$ pressure. Is this a good assumption?
An ASTM F441 chlorinated polyvinyl chloride \((\mathrm{CPVC})\) tube is embedded in a vertical concrete wall $(k=1.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\(. The wall has a height of \)1 \mathrm{~m}$, and one surface of the wall is subjected to convection with hot air at \(140^{\circ} \mathrm{C}\). The distance measured from the plate's surface that is exposed to the hot air to the tube surface is \(d=3 \mathrm{~cm}\). The ASME Code for Process Piping limits the maximum use temperature for ASTM F441 CPVC tube to $93.3^{\circ} \mathrm{C}$ (ASME B31.32014 , Table B-1). If the concrete surface that is exposed to the hot air is at \(100^{\circ} \mathrm{C}\), would the CPVC tube embedded in the wall still comply with the ASME code?
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