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On a still clear night, the sky appears to be a blackbody with an equivalent temperature of \(250 \mathrm{~K}\). What is the air temperature when a strawberry field cools to \(0^{\circ} \mathrm{C}\) and freezes if the heat transfer coefficient between the plants and air is \(6 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) because of a light breeze and the plants have an emissivity of \(0.9\) ? (a) \(14^{\circ} \mathrm{C}\) (b) \(7^{\circ} \mathrm{C}\) (c) \(3^{\circ} \mathrm{C}\) (d) \(0^{\circ} \mathrm{C}\) (e) \(-3^{\circ} \mathrm{C}\)

Short Answer

Expert verified
Answer: (c) \(3^{\circ} \mathrm{C}\)

Step by step solution

01

Define Relevant Variables and Formulae

Let's define the variables: - Convection heat transfer: \(Q_{conv}\) - Radiation heat transfer: \(Q_{rad}\) - Heat transfer coefficient: \(h=6\; \mathrm{W/m^2\cdot K}\) - Sky temperature: \(T_{sky}=250\; \mathrm{K}\) - Emissivity of plants: \(ε=0.9\) - Stefan-Boltzmann constant: \(σ = 5.67 \times 10^{-8}\; \mathrm{W/m^2\cdot K^4}\) - Plant temperature: \(T_{plant}=0^{\circ} \mathrm{C} = 273\; \mathrm{K}\) - Air temperature: \(T_{air}\), which we need to find We will use the following equations: 1. Convection heat transfer: \(Q_{conv} = hA(T_{air} - T_{plant})\) 2. Radiation heat transfer: \(Q_{rad} = εσA(T_{plant}^4 - T_{sky}^4)\) 3. Heat balance: \(Q_{conv} = Q_{rad}\)
02

Equate Convection and Radiation Heat Transfers

Using the heat balance equation, equate convection and radiation heat transfers: \(hA(T_{air} - T_{plant}) = εσA(T_{plant}^4 - T_{sky}^4)\) The area A is the same on both sides and can be canceled out, so we have: \(h(T_{air} - T_{plant}) = εσ(T_{plant}^4 - T_{sky}^4)\)
03

Solve for Air Temperature

Now we solve the equation for \(T_{air}\): \(T_{air} - T_{plant} = \frac{εσ(T_{plant}^4 - T_{sky}^4)}{h}\) \(T_{air} = T_{plant} + \frac{εσ(T_{plant}^4 - T_{sky}^4)}{h}\) Inserting the values for \(T_{plant}\), \(T_{sky}\), \(ε\), \(σ\), and \(h\), we have: \(T_{air} = 273\; \mathrm{K} + \frac{0.9(5.67 \times 10^{-8}\; \mathrm{W/m^2\cdot K^4})((273\; \mathrm{K})^4 - (250\; \mathrm{K})^4)}{6\; \mathrm{W/m^2\cdot K}}\) \(T_{air} \approx 276\; \mathrm{K}\) Now convert back to Celsius: \(T_{air} = 276\; \mathrm{K} - 273\; \mathrm{K} = 3^{\circ} \mathrm{C}\) So, the answer is (c) \(3^{\circ} \mathrm{C}\).

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Key Concepts

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

Blackbody Radiation
Blackbody radiation refers to the idealized radiant energy a perfect black body emits. A black body is a theoretical object that absorbs all radiation it encounters, and, in turn, it radiates energy at a maximum level for any given temperature. This concept is crucial in the study of thermodynamics and quantum mechanics. It's the radiation that's emitted by a body entirely based on temperature, without considering the material properties themselves, as a perfect black body does not exist in reality.

In the context of our exercise, the sky at night is treated as a black body with an equivalent temperature of 250 K. Understanding blackbody radiation helps us calculate the energy emitted by the plants as they cool down, which is significant when considering crop temperatures during a cold night.
Convection Heat Transfer
Convection heat transfer is a mode of thermal energy transportation involving the movement of fluid (which may be a liquid or gas). This motion occurs because when a fluid is heated, it becomes less dense and rises, while the cooler fluid, being denser, sinks. As a result, there is a transfer of heat from warmer areas to cooler ones.

In our strawberry field example, there's a light breeze that affects the rate of heat transfer between the air and the plants. The heat transfer coefficient, denoted by the symbol 'h' with a value of 6 W/m²·K, represents how well the air removes heat from the surfaces of the plants. A higher heat transfer coefficient indicates a greater capability to transfer heat, which can be critical in determining the air temperature necessary to prevent the strawberry field from freezing.
Radiation Heat Transfer
Radiation heat transfer is another way energy is exchanged between surfaces and their surroundings. Unlike convection, radiation does not require a medium; it can occur in a vacuum. Heat transfer by radiation is dependent on the fourth power of the temperature (according to the Stefan-Boltzmann law), making it exponentially significant at higher temperatures.

In the textbook exercise, the plants emit thermal radiation, which is described by the Stefan-Boltzmann law and depends on factors like emissivity and the temperatures of the plants and the sky. This understanding helps us identify the rate at which the plants will lose heat during the night, which is essential to predict if and when they might freeze.
Stefan-Boltzmann Constant
The Stefan-Boltzmann constant, denoted as \(\sigma\), is a fundamental physical constant in the Stefan-Boltzmann law, which calculates the power radiated from a black body in terms of its temperature. Specifically, the equation expresses the total energy radiated per unit surface area of a black body across all wavelengths per unit time. Its value is approximately \(5.67 \times 10^{-8} W/m^2\cdot K^4\).

Incorporated into the solution for our exercise, the Stefan-Boltzmann constant is key to determining the rate at which the plants lose energy by radiation to the cool night sky, which is modeled as a black body radiator.
Emissivity
Emissivity is a measure of how effectively a surface emits thermal radiation as compared to a perfect black body. The emissivity value ranges from 0 (shiny, perfect reflectors that don't emit radiation efficiently) to 1 (perfect black bodies that emit at the maximum rate for their temperature). The emissivity of a material determines how well it radiates energy in response to its temperature.

In the exercise, the strawberry plants have an emissivity of 0.9, which means they emit radiation quite efficiently, almost like a black body. This information, in conjunction with the Stefan-Boltzmann constant and the temperature difference between the sky and the plants, allows us to calculate the radiative cooling effect on the plants. Knowing the emissivity is essential for predicting the plants' temperature on a clear night and assessing the risk of freezing.

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Most popular questions from this chapter

A flat-plate solar collector is used to heat water by having water flow through tubes attached at the back of the thin solar absorber plate. The absorber plate has a surface area of \(2 \mathrm{~m}^{2}\) with emissivity and absorptivity of \(0.9\). The surface temperature of the absorber is \(35^{\circ} \mathrm{C}\), and solar radiation is incident on the absorber at \(500 \mathrm{~W} / \mathrm{m}^{2}\) with a surrounding temperature of \(0^{\circ} \mathrm{C}\). Convection heat transfer coefficient at the absorber surface is \(5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), while the ambient temperature is \(25^{\circ} \mathrm{C}\). Net heat rate absorbed by the solar collector heats the water from an inlet temperature \(\left(T_{\text {in }}\right)\) to an outlet temperature \(\left(T_{\text {out }}\right)\). If the water flow rate is \(5 \mathrm{~g} / \mathrm{s}\) with a specific heat of \(4.2 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\), determine the temperature rise of the water.

The roof of a house consists of a 22-cm-thick (st) concrete slab \((k=2 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) that is \(15 \mathrm{~m}\) wide and \(20 \mathrm{~m}\) long. The emissivity of the outer surface of the roof is \(0.9\), and the convection heat transfer coefficient on that surface is estimated to be \(15 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The inner surface of the roof is maintained at \(15^{\circ} \mathrm{C}\). On a clear winter night, the ambient air is reported to be at \(10^{\circ} \mathrm{C}\) while the night sky temperature for radiation heat transfer is \(255 \mathrm{~K}\). Considering both radiation and convection heat transfer, determine the outer surface temperature and the rate of heat transfer through the roof. If the house is heated by a furnace burning natural gas with an efficiency of 85 percent, and the unit cost of natural gas is \(\$ 1.20\) / therm ( 1 therm \(=105,500 \mathrm{~kJ}\) of energy content), determine the money lost through the roof that night during a 14-hour period.

A 4-m \(\times 5-\mathrm{m} \times 6-\mathrm{m}\) room is to be heated by one ton ( \(1000 \mathrm{~kg}\) ) of liquid water contained in a tank placed in the room. The room is losing heat to the outside at an average rate of \(10,000 \mathrm{~kJ} / \mathrm{h}\). The room is initially at \(20^{\circ} \mathrm{C}\) and \(100 \mathrm{kPa}\), and is maintained at an average temperature of \(20^{\circ} \mathrm{C}\) at all times. If the hot water is to meet the heating requirements of this room for a 24-h period, determine the minimum temperature of the water when it is first brought into the room. Assume constant specific heats for both air and water at room temperature. Answer: \(77.4^{\circ} \mathrm{C}\)

A series of experiments were conducted by passing \(40^{\circ} \mathrm{C}\) air over a long \(25 \mathrm{~mm}\) diameter cylinder with an embedded electrical heater. The objective of these experiments was to determine the power per unit length required \((\dot{W} / L)\) to maintain the surface temperature of the cylinder at \(300^{\circ} \mathrm{C}\) for different air velocities \((V)\). The results of these experiments are given in the following table: $$ \begin{array}{lccccc} \hline V(\mathrm{~m} / \mathrm{s}) & 1 & 2 & 4 & 8 & 12 \\ \dot{W} / L(\mathrm{~W} / \mathrm{m}) & 450 & 658 & 983 & 1507 & 1963 \\ \hline \end{array} $$ (a) Assuming a uniform temperature over the cylinder, negligible radiation between the cylinder surface and surroundings, and steady state conditions, determine the convection heat transfer coefficient \((h)\) for each velocity \((V)\). Plot the results in terms of \(h\left(\mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\right)\) vs. \(V(\mathrm{~m} / \mathrm{s})\). Provide a computer generated graph for the display of your results and tabulate the data used for the graph. (b) Assume that the heat transfer coefficient and velocity can be expressed in the form of \(h=C V^{m}\). Determine the values of the constants \(C\) and \(n\) from the results of part (a) by plotting \(h\) vs. \(V\) on log-log coordinates and choosing a \(C\) value that assures a match at \(V=1 \mathrm{~m} / \mathrm{s}\) and then varying \(n\) to get the best fit.

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