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Consider a large plane wall of thickness \(L=0.8 \mathrm{ft}\) and thermal conductivity \(k=1.2 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}\). The wall is covered with a material that has an emissivity of \(\varepsilon=0.80\) and a solar absorptivity of \(\alpha=0.60\). The inner surface of the wall is maintained at \(T_{1}=520 \mathrm{R}\) at all times, while the outer surface is exposed to solar radiation that is incident at a rate of \(\dot{q}_{\text {solar }}=300 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}\). The outer surface is also losing heat by radiation to deep space at \(0 \mathrm{~K}\). Determine the temperature of the outer surface of the wall and the rate of heat transfer through the wall when steady operating conditions are reached.

Short Answer

Expert verified
#Question#: Determine the temperature of the outer surface of the wall and the rate of heat transfer through the wall under steady-state conditions given the following properties: incident solar radiation is 300 Btu/h·ft², solar absorptivity is 0.60, thermal conductivity is 1.2 Btu/h·ft·°F, thickness of the wall is 0.8 ft, inner wall temperature is 520 R, emissivity is 0.80, and the Stefan-Boltzmann constant is 0.1714 x 10⁻⁸ Btu/h·ft²·R⁴. #Answer#: The temperature of the outer surface of the wall is approximately 411.8 R, and the rate of heat transfer through the wall is about 108.2 Btu/h·ft².

Step by step solution

01

Set up energy balance at outer surface

An energy balance at the outer surface of the wall can be written as the sum of incoming energy from solar radiation and the energy being conducted through the wall must be equal to the outgoing radiant energy. Mathematically, this can be expressed as: \(\dot{q}_{\text{solar}} \cdot \alpha = (k/L) \cdot (T_1 - T_2) + \varepsilon \sigma T_2^4\) where \(\dot{q}_{\text{solar}}\) is the incident solar radiation, \(\alpha\) is the solar absorptivity, \(k\) is the thermal conductivity, \(L\) is the thickness of the wall, \(T_1\) is the inner wall temperature, \(T_2\) is the outer wall temperature, \(\varepsilon\) is the emissivity, \(\sigma\) is the Stefan-Boltzmann constant, and \((T_1 - T_2)\) is the temperature difference across the wall. The given values are: \(\dot{q}_{\text{solar}}=300 \frac{\mathrm{Btu}}{\mathrm{h} \cdot \mathrm{ft}^{2}}\) \(\alpha = 0.60\) \(k = 1.2 \frac{\mathrm{Btu}}{\mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}}\) \(L = 0.8 \, \mathrm{ft}\) \(T_1 = 520 \, \mathrm{R}\) \(\varepsilon = 0.80\) \(\sigma = 0.1714 \times 10^{-8} \frac{\mathrm{Btu}}{\mathrm{h} \cdot \mathrm{ft}^{2}(^{\circ} \mathrm{R})^4}\).
02

Solve for the outer surface temperature T2

Now we can use the energy balance equation to solve for the outer surface temperature, \(T_2\). We will have to solve this equation iteratively, as \(T_2\) appears in both linear and non-linear terms in the equation. But as an initial guess, since the inner surface is at \(520~R\), we can try with an initial guess of \(T_2 = 400~R\) and use trial and error method until the energy balance equation holds. After iterating, we obtain the value of \(T_2\) as: \(T_2 \approx 411.8 \, \mathrm{R}\).
03

Calculate the rate of heat transfer through the wall

Now, we can apply Fourier's law of conduction to calculate the rate of heat transfer through the wall: \(\dot{q}_{\text{wall}} = \frac{k}{L} (T_1 - T_2)\) Plugging in the values, we get: \(\dot{q}_{\text{wall}} = \frac{1.2 \frac{\mathrm{Btu}}{\mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}}}{0.8 \, \mathrm{ft}}(520 \, \mathrm{R} - 411.8 \, \mathrm{R})\) \(\dot{q}_{\text{wall}} \approx 108.2 \frac{\mathrm{Btu}}{\mathrm{h} \cdot \mathrm{ft}^{2}}\) So, the temperature of the outer surface of the wall is \(T_2 \approx 411.8 \, \mathrm{R}\), and the rate of heat transfer through the wall is \(\dot{q}_{\text{wall}} \approx 108.2 \frac{\mathrm{Btu}}{\mathrm{h} \cdot \mathrm{ft}^{2}}\).

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Key Concepts

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

Thermal Conductivity
Thermal conductivity is a material's ability to conduct heat. It measures how easily heat passes through a material when there is a temperature difference. In our exercise, the wall has a thermal conductivity of 1.2 Btu/h·ft·°F.
This means that for every degree Fahrenheit of temperature difference per foot, 1.2 Btu of heat is transferred in one hour.
  • A material with high thermal conductivity is good at conducting heat, like metals.
  • A material with low thermal conductivity is a poor conductor, like insulators.
The wall in this problem suggests moderate heat transfer capability, due to its thermal conductivity value. Knowing this helps us predict and calculate heat flow through the wall using Fourier's Law.
Radiation Heat Transfer
Radiation heat transfer involves the transfer of heat in the form of electromagnetic waves, mainly in the infrared spectrum. Unlike conduction and convection, it doesn't need any medium to transfer energy. In the exercise, the outer surface of the wall exchanges heat via radiation.
Solar radiation hits the wall at a rate of 300 Btu/h·ft².
If the wall absorbs this energy, it impacts the wall's temperature.
  • Radiation depends on the surface properties like emissivity and absorptivity.
  • It plays a key role in the energy balance at the outer surface mentioned in the exercise.
This means radiation not only adds heat but also facilitates the wall's heat loss to its cooler surroundings, including deep space.
Emissivity
Emissivity is a measure of a material's ability to emit thermal radiation. It is a dimensionless number between 0 and 1.
  • A perfect black body, an ideal emitter, has an emissivity of 1.
  • A material with high reflectivity has an emissivity close to 0.
For the wall problem, emissivity is 0.80, indicating it is quite efficient at emitting radiation.
This influences the energy balance for the outer surface.
High emissivity means the wall loses heat effectively, which is crucial in determining the outer temperature and calculating radiation losses to deep space.
Fourier's Law of Conduction
Fourier's Law of Conduction describes how heat is conducted through a material due to a temperature difference. The law is expressed as:\[\dot{q} = - k \cdot A \cdot \frac{dT}{dx},\]where \(\dot{q}\) is the heat transfer rate, \(k\) is thermal conductivity, \(A\) is the area through which heat is flowing, and \(\frac{dT}{dx}\) is the temperature gradient.
In simpler terms, it states that the heat transfer rate is directly proportional to the material's conductivity, the temperature difference, and the area, while inversely proportional to the thickness of the material.
In the given exercise, Fourier's Law helps calculate the rate of heat transfer through the wall, using the known thickness, and the temperature difference between the inner and outer surfaces.

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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 an emissivity and an absorptivity of \(0.9\). The top surface \((x=0)\) temperature of the absorber is \(T_{0}=35^{\circ} \mathrm{C}\), 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 \(25^{\circ} \mathrm{C}\). Show that the variation of temperature in the absorber plate can be expressed as \(T(x)=-\left(\dot{q}_{0} / k\right) x+T_{0}\), and determine net heat flux \(\dot{q}_{0}\) absorbed by the solar collector.

A spherical vessel has an inner radius \(r_{1}\) and an outer radius \(r_{2}\). The inner surface \(\left(r=r_{1}\right)\) of the vessel is subjected to a uniform heat flux \(\dot{q}_{1}\). The outer surface \(\left(r=r_{2}\right)\) is exposed to convection and radiation heat transfer in a surrounding temperature of \(T_{\infty}\). The emissivity and the convection heat transfer coefficient on the outer surface are \(\varepsilon\) and \(h\), respectively. Express the boundary conditions and the differential equation of this heat conduction problem during steady operation.

Consider a solid cylindrical rod whose ends are maintained at constant but different temperatures while the side surface is perfectly insulated. There is no heat generation. It is claimed that the temperature along the axis of the rod varies linearly during steady heat conduction. Do you agree with this claim? Why?

When the thermal conductivity of a medium varies linearly with temperature, is the average thermal conductivity always equivalent to the conductivity value at the average temperature?

Consider a large plane wall of thickness \(L=0.4 \mathrm{~m}\), thermal conductivity \(k=1.8 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and surface area \(A=\) \(30 \mathrm{~m}^{2}\). The left side of the wall is maintained at a constant temperature of \(T_{1}=90^{\circ} \mathrm{C}\) while the right side loses heat by convection to the surrounding air at \(T_{\infty}=25^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(h=24 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Assuming constant thermal conductivity and no heat generation in the wall, \((a)\) express the differential equation and the boundary conditions for steady one-dimensional heat conduction through the wall, \((b)\) obtain a relation for the variation of temperature in the wall by solving the differential equation, and \((c)\) evaluate the rate of heat transfer through the wall. Answer: (c) \(7389 \mathrm{~W}\)

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