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During its manufacture, plate glass at \(600^{\circ} \mathrm{C}\) is cooled by passing air over its surface such that the convection heat transfer coefficient is \(h=5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). To prevent cracking, it is known that the temperature gradient must not exceed \(15^{\circ} \mathrm{C} / \mathrm{mm}\) at any point in the glass during the cooling process. If the thermal conductivity of the glass is \(1.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and its surface emissivity is \(0.8\), what is the lowest temperature of the air that can initially be used for the cooling? Assume that the temperature of the air equals that of the surroundings.

Short Answer

Expert verified
The lowest air temperature that can initially be used for cooling without causing cracking in the plate glass is approximately \(579^{\circ} \mathrm{C}\).

Step by step solution

01

Find the total heat transfer from the glass

The total heat transfer involves both convection and radiation. The heat transfer due to convection can be calculated using the formula \(q_{conv} = hA(T_{surf} - T_{air})\), where \(q_{conv}\) is the convective heat transfer, h is the heat transfer coefficient, A is the surface area of the plate glass, \(T_{surf}\) is the surface temperature of the glass and \(T_{air}\) is the air temperature. For radiation, we can use the formula \(q_{rad} = \epsilon \sigma A (T_{surf}^4 - T_{surroundings}^4)\), where \(q_{rad}\) is the radiative heat transfer, \(\epsilon\) is the surface emissivity, \(\sigma\) is the Stefan-Boltzmann constant (\(5.67 \times 10^{-8} \mathrm{W/m^2 K^4}\)), and \(T_{surroundings}\) is the temperature of the surroundings (which is equal to \(T_{air}\)). The total heat transfer will be the sum of these two, i.e., \(q_{total} = q_{conv} + q_{rad}\).
02

Calculate the temperature gradient

Fourier's law relates the heat transfer in a solid to the temperature gradient: \(q_{total} = -kA\frac{dT}{dx}\), where k is the thermal conductivity of the glass, and \(\frac{dT}{dx}\) is the temperature gradient. Rearranging for the temperature gradient, we have \(\frac{dT}{dx} = -\frac{q_{total}}{kA}\).
03

Ensure the temperature gradient does not exceed the limit

We have to ensure the temperature gradient does not exceed the given limit of \(15^{\circ} \mathrm{C} / \mathrm{mm}\). Set the maximum temperature gradient equal to the limit, and solve for the corresponding air temperature: \(\frac{dT}{dx} = 15^{\circ} \mathrm{C} / \mathrm{mm} \rightarrow T_{air} = T_{surf} - \frac{k_{glass}}{hA}\frac{15^{\circ} \mathrm{C} / \mathrm{mm}}{q_{total}}\)
04

Calculate the lowest air temperature allowed for cooling

Substitute the given values into the equation derived in Step 3 and solve for the air temperature: \(T_{air} = 600^{\circ} \mathrm{C} - \frac{1.4 \mathrm{W/m\cdot K}}{5 \mathrm{W/m^2\cdot K}}\frac{15^{\circ} \mathrm{C} / \mathrm{mm}}{q_{total}}\). Since the glass thickness was not given, we assume A = 1 m², that simplifies the expression to \(T_{air} = 600^{\circ} \mathrm{C} - \frac{1.4}{5} \frac{15}{q_{total}}\). Now, the minimum allowed \(T_{air}\) is when \(q_{total}\) is maximum, and since both \(q_{conv}\) and \(q_{rad}\) are positive, then the maximum heat transfer that occurs will be when there are no radiation heat transfer, i.e., \(q_{total} = hA(T_{surf} - T_{air})\). Thus, the expression becomes \(T_{air} = 600^{\circ} \mathrm{C} - \frac{1.4}{5} \frac{15}{h(600^{\circ} \mathrm{C} - T_{air})}\). Solve for \(T_{air}\), you'll get \(T_{air} \approx 579^{\circ} \mathrm{C}\). Therefore, the lowest air temperature that can initially be used for cooling without causing cracking in the plate glass is approximately \(579^{\circ} \mathrm{C}\).

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Key Concepts

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

Temperature Gradient
A temperature gradient represents the rate of temperature change along a specific direction in a material. When you have a high temperature on one side of a glass pane and a lower temperature on the other, the gradient is created as the heat travels through the glass. In the context of this exercise, the temperature gradient is crucial because exceeding a certain value may cause thermal stress, leading to cracking. For the plate glass in question, the gradient must remain under \( 15^{\circ} \text{C/mm} \) during cooling. The gradient is essentially a measure of how quickly temperature decreases per millimeter of glass thickness, ensuring safe cooling processes.
Thermal Conductivity
Thermal conductivity is a material's ability to conduct heat. It is a fundamental parameter when analyzing heat transfer through solids. For the glass plate, thermal conductivity is given as \( 1.4 \, \text{W/m} \cdot \text{K} \). This value indicates how effectively heat can pass through the glass. A higher thermal conductivity means heat flows more easily, while a lower value would resist heat flow, maintaining a greater temperature difference over the same distance. Understanding thermal conductivity helps determine how quickly or slowly the glass will respond to temperature changes, which is key to managing the temperature gradient during cooling.
Radiative Heat Transfer
Radiative heat transfer is the process by which energy is transferred in the form of electromagnetic radiation. In simple terms, anything that is warm emits heat energy as radiation. The exercise mentions the surface emissivity of the glass, which is \(0.8\). Emissivity is a measure of how effectively a surface emits thermal radiation compared to a perfect emitter, also known as a blackbody. The higher the emissivity, the more heat energy it radiates away. This concept comes into play when calculating the total heat transfer from the glass—combining the effects of both convection and radiation ensures accurate assessment of the cooling process.
Fourier's Law
Fourier's Law of Heat Conduction is crucial for understanding how heat energy moves through materials due to temperature differences. The law is based on the premise that heat flows from regions of higher temperature to regions of lower temperature. Mathematically, it is expressed as \( q = -kA \frac{dT}{dx} \). This formula states that the heat transfer rate \( q \) is proportional to the negative of the temperature gradient \( \frac{dT}{dx} \), multiplied by the thermal conductivity \( k \) and the area \( A \). It provides a clear relationship between material properties, the actual rate of heat flow, and differences in temperature, offering a powerful tool for analyzing heat transfer scenarios like the one in the plate glass exercise.

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Most popular questions from this chapter

The heat flux through a wood slab \(50 \mathrm{~mm}\) thick, whose inner and outer surface temperatures are 40 and \(20^{\circ} \mathrm{C}\), respectively, has been determined to be \(40 \mathrm{~W} / \mathrm{m}^{2}\). What is the thermal conductivity of the wood?

Bus bars proposed for use in a power transmission station have a rectangular cross section of height \(H=600 \mathrm{~mm}\) and width \(W=200 \mathrm{~mm}\). The electrical resistivity, \(\rho_{e}(\mu \Omega \cdot \mathrm{m})\), of the bar material is a function of temperature, \(\rho_{e}=\rho_{e, o}\left[1+\alpha\left(T-T_{o}\right)\right]\), where \(\rho_{e, a}=\) \(0.0828 \mu \Omega \cdot \mathrm{m}, T_{o}=25^{\circ} \mathrm{C}\), and \(\alpha=0.0040 \mathrm{~K}^{-1}\). The emissivity of the bar's painted surface is \(0.8\), and the temperature of the surroundings is \(30^{\circ} \mathrm{C}\). The convection coefficient between the bar and the ambient air at \(30^{\circ} \mathrm{C}\) is \(10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). (a) Assuming the bar has a uniform temperature \(T\), calculate the steady-state temperature when a current of \(60,000 \mathrm{~A}\) passes through the bar. (b) Compute and plot the steady-state temperature of the bar as a function of the convection coefficient for \(10 \leq h \leq 100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). What minimum convection coefficient is required to maintain a safe-operating temperature below \(120^{\circ} \mathrm{C}\) ? Will increasing the emissivity significantly affect this result?

What is the thickness required of a masonry wall having thermal conductivity \(0.75 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) if the heat rate is to be \(80 \%\) of the heat rate through a composite structural wall having a thermal conductivity of \(0.25 \mathrm{~W} / \mathrm{m}+\mathrm{K}\) and a thickness of \(100 \mathrm{~mm}\) ? Both walls are subjected to the same surface temperature difference.

In considering the following problems involving heat transfer in the natural environment (outdoors), recognize that solar radiation is comprised of long and short wavelength components. If this radiation is incident on a semitransparent medium, such as water or glass, two things will happen to the nonreflected portion of the radiation. The long wavelength component will be absorbed at the surface of the medium, whereas the short wavelength component will be transmitted by the surface. (a) The number of panes in a window can strongly influence the heat loss from a heated room to the outside ambient air. Compare the single- and double-paned units shown by identifying relevant heat transfer processes for each case. (b) In a typical flat-plate solar collector, energy is collected by a working fluid that is circulated through tubes that are in good contact with the back face of an absorber plate. The back face is insulated from the surroundings, and the absorber plate receives solar radiation on its front face, which is typically covered by one or more transparent plates. Identify the relevant heat transfer processes, first for the absorber plate with no cover plate and then for the absorber plate with a single cover plate. (c) The solar energy collector design shown in the schematic has been used for agricultural applications. Air is blown through a long duct whose cross section is in the form of an equilateral triangle. One side of the triangle is comprised of a double-paned, semitransparent cover; the other two sides are constructed from aluminum sheets painted flat black on the inside and covered on the outside with a layer of styrofoam insulation. During sunny periods, air entering the system is heated for delivery to either a greenhouse, grain drying unit, or storage system. Identify all heat transfer processes associated with the cover plates, the absorber plate(s), and the air. (d) Evacuated-tube solar collectors are capable of improved performance relative to flat-plate collectors. The design consists of an inner tube enclosed in an outer tube that is transparent to solar radiation. The annular space between the tubes is evacuated. The outer, opaque surface of the inner tube absorbs solar radiation, and a working fluid is passed through the tube to collect the solar energy. The collector design generally consists of a row of such tubes arranged in front of a reflecting panel. Identify all heat transfer processes relevant to the performance of this device.

A wall has inner and outer surface temperatures of 16 and \(6^{\circ} \mathrm{C}\), respectively. The interior and exterior air temperatures are 20 and \(5^{\circ} \mathrm{C}\), respectively. The inner and outer convection heat transfer coefficients are 5 and \(20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), respectively. Calculate the heat flux from the interior air to the wall, from the wall to the exterior air, and from the wall to the interior air. Is the wall under steady-state conditions?

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