/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 118 The lower side of a \(400-\mathr... [FREE SOLUTION] | 91Ó°ÊÓ

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The lower side of a \(400-\mathrm{mm}\)-diameter disk is heated by an electric furnace, while the upper side is exposed to quiescent, ambient air and sumoundings at \(300 \mathrm{~K}\). The radiant furnace (negligible convection) is of circular construction with the bottoen surface \(\left(\alpha_{1}-0.6\right)\) and cylindrical side surface \(\left(\varepsilon_{1}=1.0\right)\) maintained af \(T_{1}=T_{2}=500 \mathrm{~K}\). The surface of the disk facing the radiant furnace is black \(\left(\varepsilon_{d, 1}=1.0\right)\). while the upper surface has an emissivity of \(\varepsilon_{d, 2}=0.8\). Assume the plate and furnace surfaces to be diffuse and gray. (a) Determine the net heat transfer rate to the disk, \(q_{\text {nated, when }} T_{d}=400 \mathrm{~K}\). (b) Plot \(q_{\text {netd as a }}\) a function of the disk temperature for \(300 \leq T_{a} \leq 500 \mathrm{~K}\), with all other conditions remaining the same. What is the steady-state temperature of the disk?

Short Answer

Expert verified
The net heat transfer rate to the disk when the disk temperature is \(400 \mathrm{~K}\) is \(5.019 × 10^3 W/m^2\). By plotting the net heat transfer rate as a function of disk temperature between \(300 \mathrm{~K}\) and \(500 \mathrm{~K}\), the steady-state temperature of the disk can be found by observing where the net heat transfer intersects the x-axis. The steady-state temperature will indicate that the disk is maintaining a constant temperature.

Step by step solution

01

Find the radiation heat transfer to the disk

To find the radiation heat transfer to the disk, we will use the Stefan-Boltzmann law, which states: \(q = \varepsilon \sigma (T_{furnace}^4 - T_{disk}^4)\) Here, \(\varepsilon\) is the emissivity, \(\sigma\) is the Stefan-Boltzmann constant (\(5.67×10^{-8} W/m^2K^4\)), and \(T\) is the temperature in Kelvin. Since the emissivities are different on each side of the disk, we must account for them separately. For the bottom surface facing the radiant furnace, the radiation heat transfer is: \(q_{1} = \varepsilon_{d1} \sigma (T_{1}^4 - T_{d}^4)\) For the top surface, the radiation heat transfer is: \(q_{2} = \varepsilon_{d2} \sigma (T_{2}^4 - T_{d}^4)\)
02

Calculate the heat transfer rates for the given temperatures

We are given the following temperatures: \(T_{1} = T_{2} = 500K\), \(T_{d} = 400K\), and \(T_{a} = 300K\). We are also given the emissivities: \(\varepsilon_{d1} = 1.0\) and \(\varepsilon_{d2} = 0.8\). Since the ambient surroundings are at 300 K, we must also account for the radiation heat transfer from the top surface of the disk to the ambient surroundings: \(q_{3} = \varepsilon_{d2} \sigma (T_{a}^4 - T_{d}^4)\) Now we can calculate the heat transfer rates for the given temperatures: \(q_{1} = 1.0(5.67×10^{-8})(500^4 - 400^4) = 3.605 × 10^3 W/m^2\) \(q_{2} = 0.8(5.67×10^{-8})(500^4 - 400^4) = 2.884 × 10^3 W/m^2\) \(q_{3} = 0.8(5.67×10^{-8})(300^4 - 400^4) = -1.470 × 10^3 W/m^2\)
03

Find the net heat transfer rate to the disk

To find the net heat transfer rate to the disk, we will add up the heat transfer rates calculated in the previous step: \(q_{net} = q_{1} + q_{2} + q_{3} = 3.605 × 10^3 + 2.884 × 10^3 + (-1.470 × 10^3) = 5.019 × 10^3 W/m^2\)
04

Plot the net heat transfer rate as a function of disk temperature

To plot the net heat transfer as a function of disk temperature, we will need to substitute a range of disk temperatures (300 K to 500 K) into the equations from step 1 and step 3: \(q_{net}(T_{d}) = \varepsilon_{d1}\sigma(T_{1}^4 - T_{d}^4) + \varepsilon_{d2}\sigma(T_{2}^4 - T_{d}^4) - \varepsilon_{d2}\sigma(T_{a}^4 - T_{d}^4)\) Once the plot is created, we will look for the steady-state temperature, which occurs when the net heat transfer to the disk is zero (i.e., the heat transfer rate in equals the heat transfer rate out). By plotting the equation and observing where the net heat transfer intersects the x-axis, the steady-state temperature of the disk can be found. We will be using specialized software or graphing calculators to achieve this.
05

Determine the steady-state temperature of the disk

After plotting q_net as a function of the disk temperature and finding where it intersects the x-axis, we will get the steady-state temperature of the disk. This steady-state temperature will indicate that the disk is neither heating nor cooling and is maintaining a constant temperature. The final answer will vary depending on the software and plot used, but by following the procedure outlined in this solution, it should be possible to find the steady-state temperature of the disk.

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Key Concepts

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

Stefan-Boltzmann Law
The Stefan-Boltzmann Law is a fundamental principle for understanding radiation heat transfer. It states that the power radiated per unit area of a black body is directly proportional to the fourth power of its absolute temperature. This can be expressed by the formula: \( q = \varepsilon \sigma T^4 \), where \( q \) represents the radiant energy emitted per unit area, \( \varepsilon \) is the emissivity of the material, \( \sigma \) is the Stefan-Boltzmann constant approximately equal to \( 5.67 \times 10^{-8} W/m^2K^4 \), and \( T \) represents the absolute temperature in Kelvin.
  • For perfect black bodies \( (\varepsilon = 1) \), the law defines that the radiant power is at its maximum as all radiation at that temperature is emitted.
  • In typical applications, surfaces are not perfect black bodies, and their emissivity \( (\varepsilon) \) is less than 1.
The law is useful in our exercise since it helps us calculate the radiant heat transfer from the surfaces of the disk when different emissivities are involved. By comparing the heat emitted by the furnace and the disk, students can determine the net heat transfer over the disk surface.
Emissivity
Emissivity is a material property that measures a surface's ability to emit thermal radiation compared to a perfect black body at the same temperature, and it ranges from 0 to 1.
  • If \( \varepsilon = 1 \), the surface is a perfect emitter (like a black body).
  • If \( \varepsilon = 0 \), the surface does not emit thermal radiation.
In the exercise, the emissivity values \( \varepsilon_{d1} \) and \( \varepsilon_{d2} \) determine how each side of the disk interacts with thermal radiation. The bottom side of the disk, facing the furnace, is treated as a perfect emitter (\( \varepsilon_{d1} = 1.0 \)), absorbing and emitting radiation efficiently. However, the upper side, exposed to cooler ambient air, has an emissivity of \( \varepsilon_{d2} = 0.8 \), allowing it to emit less than a perfect black body would. Understanding emissivity is crucial for calculating the net rate of heat transfer, where both sides contribute differently to the system's energy balance because they radiate differently.
Steady-State Temperature
The concept of steady-state temperature refers to a condition where the temperature of the system remains constant over time. In the context of the exercise, it occurs when the net heat transfer to or from the disk reaches zero. This means that the heat entering the disk equals the heat leaving it. In practical terms:
  • Energy balance is achieved: input and output energy flows are equal.
  • The system does not experience any temperature changes with time.
To find the steady-state temperature in the exercise, students need to analyze when the computed net heat transfer becomes zero using the net heat transfer equation. By adjusting the temperature of the disk \( (T_d) \) and recalculating the net heat transfer, students can identify the point where the disk neither gains nor loses heat. Achieving this balance ensures the system is in equilibrium, predicting realistic behavior in thermal systems.

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Most popular questions from this chapter

A flat-bottomed hole \(6 \mathrm{~mm}\) in diameter is bored to a depth of \(24 \mathrm{~mm}\) in a diffuse, gray material having an emissivity of \(0.8\) and a uniform temperature of \(1000 \mathrm{~K} .\) (a) Determine the radiant power leaving the opening of the cavity. (b) The effective emissivity \(\varepsilon_{e}\) of a cavity is defined as the ratio of the radiant power leaving the cavity to that from a blackbody having the area of the cavity opening and a temperature of the inner surfaces of the cavity. Calculate the effective emissivity of the cavity described above. (c) If the depth of the hole were increased, would \(\varepsilon_{e}\) increase or decrease? What is the limit of \(s_{\epsilon}\) as the depth increases?

Many products are processed in a manner that requires a specified product temperature as a function of time. Consider a product in the shape of long, 10-mmdiameter cylinders that are conveyed slowly through a processing oven as shown in the schematic. The product exhibits near-black behavior and is attached to the conveying apparatus at the product's ends. The surroundings are at \(300 \mathrm{~K}\), while the radiation panel heaters are each isothermal at \(500 \mathrm{~K}\) and have surfaces that exhibit near-black behavior. An engineer proposes a novel oven design with a tilting top surface so as to be able to quickly change the thermal response of the product. (a) Determine the radiation per unit length incident upon the product at \(x=0.5 \mathrm{~m}\) and \(x=1 \mathrm{~m}\) for \(a=0\). (b) Determine the radiation per unit length incident upon the product at \(x=0.5 \mathrm{~m}\) and \(x=1 \mathrm{~m}\) for \(\alpha=\pi / 15\). Hint: The view factor from the cylinder to the left-hand side surroundings can be found by summing the view factors from the cylinder to the two surfaces shown as red dashed lines in the schematic.

Consider two large, diffuse, gray, parallel surfaces separated by a small distance. If the surface emissivities are \(0.8\), what emissivity should a thin radiation shield have to reduce the radiation heat transfer rate between the two surfaces by a factor of 10 ?

A novel infrared recycler has been proposed for reclaiming the millions of kilograms of waste plastics produced by the dismantling and shredding of automotive vehicles following their refirement. To address the problem of sorting mixed plastics into components such as polypropylene and polycarbonate, a washed stream of the mixed plastics is routed to an infrared heating system, where it is dried and stbsequently heated to a temperature for which one of the components begins to soften, while the others remain rigid. The mixed stream is then routed through steel rollers, to which the softened plastic sticks and is removed from the stream. Heating of the stream is then continued to facilitate removal of a second component, and the heating/removal process is repeated until all of the components are separated. Consider the initial drying stage for a system comprised of a cylindrical heater aligned coaxially with a rotating drum of diameter \(D_{d}=1 \mathrm{~m}\). Shortly after entering the drum, wet plastic pellets may be assumed to fully cover the bottom semicylindrical section and to remain at a temperature of \(T_{p}=\) \(325 \mathrm{~K}\) during the drying process. The surface area of the pellets may be assumed to correspond to that of the semicylinder and to have an emissivity of \(\varepsilon_{p}=0.95\). (a) If the flow of dry air through the drum maintains a convection mass transfer coefficient of \(0.024 \mathrm{~m} / \mathrm{s}\) on the surface of the pellets, what is the evaporation rate per unit length of the drum? (b) Neglecting convection heat transfer, determine the temperature \(T_{b}\) that must be maintained by a heater of diameter \(D_{\mathrm{b}}=0.10 \mathrm{~m}\) and emissivity \(\varepsilon_{h}=0.8\) to sustain the foregoing evaporation rate. What is the corresponding value of the temperature \(T_{d}\) for the top surface of the drum? The outer surface of the dram is well insulated, and its length-to-diameter ratio is large. As applied to the top \((d)\) or bottom \((p)\) surface of the drum, the view factor of an infinitely long semicylinder to itself, in the presence of a concentric, coaxial cylinder, may be expressed as $$ \begin{aligned} F_{U}=& 1-\frac{2}{\pi}\left\\{\left[1-\left(D_{d} / D_{d}\right)^{2}\right]^{1 / 2}\right.\\\ &\left.+\left(D_{k} / D_{d}\right) \sin ^{-1}\left(D_{h} / D_{d}\right)\right\\} \end{aligned} $$

A cryogenic fluid flows through a tube \(20 \mathrm{~mm}\) in diameter, the outer surface of which is diffuse and gray with an emissivity of \(0.02\) and temperature of \(77 \mathrm{~K}\). This tube is concentric with a larger tube of 50 \(\mathrm{mm}\) diameter, the inner surface of which is diffuse and gray with an emissivity of \(0.05\) and temperature of \(300 \mathrm{~K}\). The space between the surfaces is evacuated. Determine the heat gain by the cryogenic fluid per unit length of the inner tube. If a thin-walled radiation shield that is diffuse and gray with an emissivity of \(0.02\) (both sides) is inserted midway between the inner and outer surfaces, calculate the change (percentage) in heat gain per unit length of the inner tube.

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