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Consider a flat-plate solar collector placed horizontally on the flat roof of a house. The collector is \(5 \mathrm{ft}\) wide and \(15 \mathrm{ft}\) long, and the average temperature of the exposed surface of the collector is \(100^{\circ} \mathrm{F}\). The emissivity of the exposed surface of the collector is \(0.9\). Determine the rate of heat loss from the collector by convection and radiation during a calm day when the ambient air temperature is \(70^{\circ} \mathrm{F}\) and the effective sky temperature for radiation exchange is \(50^{\circ} \mathrm{F}\). Take the convection heat transfer coefficient on the exposed surface to be $2.5 \mathrm{Btu} / \mathrm{h} . \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}$.

Short Answer

Expert verified
Answer: The rate of heat loss from the solar collector by convection and radiation during a calm day is approximately 5931.31 Btu/h.

Step by step solution

01

Calculate the area of the collector

First, we need to find the area of the solar collector. The given dimensions are 5 ft wide and 15 ft long. Multiply the width by the length to find the total area: A = width × length = (5 ft) × (15 ft) = 75 ft^2.
02

Calculate the heat transfer rate due to convection

We are given the convection heat transfer coefficient, h, the surface temperature, Ts, and the ambient air temperature, T_inf. We can use the following formula to calculate the heat transfer rate due to convection, Q_conv: Q_conv = h × A × (Ts - T_inf) Plug in the known values: Q_conv = (2.5 Btu/h.ft^2.°F) × (75 ft^2) × (100°F - 70°F) = 2.5 × 75 × 30 = 5625 Btu/h
03

Calculate the heat transfer rate due to radiation

Now we need to find the heat transfer rate due to radiation, Q_rad. We are given the emissivity, ε, and the surface temperature, Ts, as well as the effective sky temperature, T_sky. We will use the Stefan-Boltzmann constant, σ, which is equal to 0.1714×10^{-8} Btu/h.ft^2.°R^4. Remember to convert temperatures to absolute temperature (Rankine) for radiation calculations. We can use the following formula to calculate Q_rad: Q_rad = ε × σ × A × (Ts^4 - T_sky^4) Convert temperatures to Rankine: Ts_R = 100°F + 459.67 = 559.67°R T_sky_R = 50°F + 459.67 = 509.67°R Plug in the known values: Q_rad = 0.9 × (0.1714×10^{-8} Btu/h.ft^2.°R^4) × (75 ft^2) × (559.67^4 - 509.67^4) ≈ 306.31 Btu/h
04

Calculate the total heat loss rate

Now, we sum the heat transfer rates due to convection and radiation to find the total heat loss rate, Q_total: Q_total = Q_conv + Q_rad = 5625 Btu/h + 306.31 Btu/h ≈ 5931.31 Btu/h The rate of heat loss from the solar collector by convection and radiation during a calm day is approximately 5931.31 Btu/h.

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Most popular questions from this chapter

The boiling temperature of nitrogen at atmospheric pressure at sea level $(1 \mathrm{~atm})\( is \)-196^{\circ} \mathrm{C}$. Therefore, nitrogen is commonly used in low-temperature scientific studies since the temperature of liquid nitrogen in a tank open to the atmosphere remains constant at $-196^{\circ} \mathrm{C}$ until the liquid nitrogen in the tank is depleted. Any heat transfer to the tank results in the evaporation of some liquid nitrogen, which has a heat of vaporization of \(198 \mathrm{~kJ} / \mathrm{kg}\) and a density of \(810 \mathrm{~kg} / \mathrm{m}^{3}\) at \(1 \mathrm{~atm}\). Consider a 4-m-diameter spherical tank initially filled with liquid nitrogen at \(1 \mathrm{~atm}\) and \(-196^{\circ} \mathrm{C}\). The tank is exposed to \(20^{\circ} \mathrm{C}\) ambient air with a heat transfer coefficient of $25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. The temperature of the thin- shelled spherical tank is observed to be almost the same as the temperature of the nitrogen inside. Disregarding any radiation heat exchange, determine the rate of evaporation of the liquid nitrogen in the tank as a result of the heat transfer from the ambient air.

A 3 -m-internal-diameter spherical tank made of \(1-\mathrm{cm}\) thick stainless steel is used to store iced water at \(0^{\circ} \mathrm{C}\). The tank is located outdoors at \(25^{\circ} \mathrm{C}\). Assuming the entire steel tank to be at \(0^{\circ} \mathrm{C}\) and thus the thermal resistance of the tank to be negligible, determine \((a)\) the rate of heat transfer to the iced water in the tank and (b) the amount of ice at \(0^{\circ} \mathrm{C}\) that melts during a 24 -h period. The heat of fusion of water at atmospheric pressure is \(h_{i f}=333.7 \mathrm{~kJ} / \mathrm{kg}\). The emissivity of the outer surface of the tank is \(0.75\), and the convection heat transfer coefficient on the outer surface can be taken to be $30 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Assume the average surrounding surface temperature for radiation exchange to be \(15^{\circ} \mathrm{C}\). Answers: (a) \(23.1 \mathrm{~kW}\), (b) \(5980 \mathrm{~kg}\)

A solid plate, with a thickness of \(15 \mathrm{~cm}\) and a thermal conductivity of \(80 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), is being cooled at the upper surface by air. The air temperature is $10^{\circ} \mathrm{C}$, while the temperatures at the upper and lower surfaces of the plate are 50 and \(60^{\circ} \mathrm{C}\), respectively. Determine the convection heat transfer coefficient of air at the upper surface, and discuss whether the value is reasonable or not for forced convection of air.

A cold bottled drink ( $\left.m=2.5 \mathrm{~kg}, c_{p}=4200 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( at \)5^{\circ} \mathrm{C}$ is left on a table in a room. The average temperature of the drink is observed to rise to \(15^{\circ} \mathrm{C}\) in \(30 \mathrm{~min}\). The average rate of heat transfer to the drink is (a) \(23 \mathrm{~W}\) (b) \(29 \mathrm{~W}\) (c) \(58 \mathrm{~W}\) (d) \(88 \mathrm{~W}\) (e) \(122 \mathrm{~W}\)

Write an essay on how microwave ovens work, and explain how they cook much faster than conventional ovens. Discuss whether conventional electric or microwave ovens consume more electricity for the same task.

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