/*! 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 108 Applying high-emissivity paints ... [FREE SOLUTION] | 91Ó°ÊÓ

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Applying high-emissivity paints to radiating surfaces is a common technique used to enhance heat transfer by radiation. (a) For large parallel plates, determine the radiation heat flux across the gap when the surfaces are at \(T_{1}=350 \mathrm{~K}, T_{2}=300 \mathrm{~K}, \varepsilon_{1}=\varepsilon_{2}=\varepsilon_{x}=0.85 .\) (b) Determine the radiation heat flux when a very thin layer of high- emissivity paint, \(\varepsilon_{p}=0.98\), is applied to both surfaces. (c) Determine the radiation heat flux when the paint layers are each \(L=2 \mathrm{~mm}\) thick and the thermal conductivity of the paint is \(k=0.21 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). (d) Plot the heat flux across the gap for the bare surface as a function of \(\varepsilon_{x}\) with \(0.05 \leq \varepsilon_{x} \leq 0.95\). Show on the same plot the heat flux for the painted surface with very thin paint layers and the painted surface with \(L=2\)-mm-thick paint layers.

Short Answer

Expert verified
In summary, we calculated the radiation heat flux between two large parallel plates with different surface temperatures and emissivities using the radiation heat transfer formula. First, we calculated the heat flux for the bare surfaces (\(q\)), then for surfaces with a very thin layer of high-emissivity paint (\(q_p\)), and finally for surfaces with 2-mm-thick paint layers (\(q_{th}\)), considering the thermal resistance of the paint layers. Lastly, we were asked to plot the heat flux across the gap as a function of surface emissivity (\(\varepsilon_x\)) for the bare surface, the very thin paint layer, and the 2-mm-thick paint layer surfaces.

Step by step solution

01

Determine the effective emissivity for parallel surfaces

The effective emissivity for parallel surfaces is given by: \[\frac{1}{\varepsilon_{\text{eff}}} = \frac{1-\varepsilon_x}{\varepsilon_x}\] With \(\varepsilon_x = 0.85\), we can calculate \(\varepsilon_\text{eff}\): \[\varepsilon_{\text{eff}} = \frac{\varepsilon_x}{1+\varepsilon_x - \varepsilon_x^2} = \frac{0.85}{1+0.85 - 0.85^2}\]
02

Calculate the radiation heat flux

To determine the radiation heat flux across the gap, we will use the radiation heat transfer formula: \[q = \varepsilon_\text{eff}\sigma(T_1^4 - T_2^4)\] Where \(\sigma\) is the Stefan-Boltzmann constant, \(\sigma = 5.67\times10^{-8} Wm^{-2}K^{-4}\). Using the given values for \(T_1 = 350K\) and \(T_2 = 300K\), we can calculate the radiation heat flux, \(q\). (b) Determine the radiation heat flux with a very thin layer of high-emissivity paint
03

Determine the effective emissivity with the paint layer

First, we need to determine the effective emissivity for each surface with the paint layer. Using the formula for the effective emissivity between two layers: \[\frac{1}{\varepsilon_{\text{eff}}} = \frac{1-\varepsilon_p}{\varepsilon_p} + \frac{1-\varepsilon_x}{\varepsilon_x}\] With \(\varepsilon_p = 0.98\), we can calculate the new \(\varepsilon_\text{eff}\).
04

Calculate the radiation heat flux with the paint layer

Now, we can use the same radiation heat transfer formula from step 2(a) but with the new effective emissivity to calculate the radiation heat flux, \(q_p\). (c) Determine the radiation heat flux when the paint layers are each 2mm thick
05

Determine the thermal resistance of the paint layers

To determine the radiation heat flux with the paint layers of thickness \(L=2mm=0.002m\), we need to calculate the thermal resistance of the paint layers. This can be done using the formula: \[R = \frac{L}{kA}\] Where \(R\) is the thermal resistance, \(k = 0.21W/m\cdot K\) is the thermal conductivity of the paint, and \(A\) is the surface area of each plate.
06

Calculate the radiation heat flux with thick paint layers

Using the thermal resistance, we can modify the radiation heat transfer formula to account for the thick paint layers. The formula with thermal resistance becomes: \[q_{th} = \frac{\varepsilon_\text{eff}\sigma(T_1^4 - T_2^4)}{1+\frac{R_1+R_2}{A}}\] Using the values for \(\varepsilon_\text{eff}\) calculated in part (b), we can calculate the radiation heat flux \(q_{th}\) when the paint layers are 2mm thick. (d) Plot the heat flux across the gap for the bare surface as a function of \(\varepsilon_x\) To solve this part, we will use the same formulas as in part (a) and (b), but we'll vary \(\varepsilon_x\) from 0.05 to 0.95 to plot the heat flux for the bare surface, the very thin paint layer, and the 2-mm-thick paint layer surfaces. The plot will present the heat flux as a function of different values of \(\varepsilon_x\).

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Key Concepts

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

Emissivity
Emissivity is a measure of a material's ability to emit thermal radiation compared to a perfect black body, which has an emissivity of 1. In simple terms, it indicates how effectively a surface can radiate energy. Materials with high emissivity can radiate heat more efficiently than those with low emissivity.

Considering the exercise scenario, applying high-emissivity paints to a surface amplifies its radiation heat transfer capabilities. The effective emissivity, denoted as \( \varepsilon_\text{eff} \) in the solution, plays a crucial role in determining the radiation heat flux between two surfaces. It's a combined property that takes into account the emissivities of both radiating surfaces or layers, as seen with \( \varepsilon_x \) for the surfaces and \( \varepsilon_p \) for the paint. By enhancing emissivity using a paint like \( \varepsilon_p = 0.98 \) we significantly increase the heat flux across the gap.
Stefan-Boltzmann Constant
The Stefan-Boltzmann constant, represented by \( \sigma \) and valued at \( 5.67\times10^{-8} \text{Wm}^{-2}\text{K}^{-4} \) is fundamental in quantifying radiation heat transfer. It links the temperature of an object to the total emitted radiation.

The Stefan-Boltzmann law explains how the thermal radiation emitted by a black body is proportional to the fourth power of its temperature. For real-world applications, the law incorporates the emissivity factor to account for the less-than-perfect radiation of materials. In the solution provided, \( \sigma \) is used in the formula \( q = \varepsilon_\text{eff}\sigma(T_1^4 - T_2^4) \) to calculate the radiation heat flux between two surfaces at different temperatures.
Thermal Resistance
Thermal resistance is a measure of a material's opposition to heat flow through it, often denoted by \( R \) in equations. It's equivalent to electrical resistance in the context of heat transfer. The higher the thermal resistance, the more the material impedes heat transfer.

This concept is particularly critical when considering conductive heat transfer, as seen when the exercise introduces a paint layer with thickness \( L \) and thermal conductivity \( k \) in its calculations. The formula used, \( R = \frac{L}{kA} \) where \( A \) denotes the area, allows us to determine the thermal resistance of the paint layers, which is an essential step in calculating the overall heat flux when these layers are considered.
Conductive Heat Transfer
Conductive heat transfer refers to the transfer of heat through a material due to a temperature gradient. It's a fundamental mode of thermal energy movement within solids or between solid objects in contact. Materials with high thermal conductivity can rapidly transfer heat, unlike those with low conductivity that act as insulators.

In the given exercise, the thermal conductivity \( k \) of the paint affects how the applied layers alter the conductive heat transfer. The additional thermal resistance introduced by the paint layers is calculated and factored into the modified radiation heat transfer formula, \( q_{th} = \frac{\varepsilon_\text{eff}\sigma(T_1^4 - T_2^4)}{1+\frac{R_1+R_2}{A}} \) to find the heat flux \( q_{th} \) across the gap. Conductive heat transfer combined with surface emissivity changes how the overall system releases heat.

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Most popular questions from this chapter

The arrangement shown is to be used to calibrate a heat flux gage. The gage has a black surface that is \(10 \mathrm{~mm}\) in diameter and is maintained at \(17^{\circ} \mathrm{C}\) by means of a water-cooled backing plate. The heater, \(200 \mathrm{~mm}\) in diameter, has a black surface that is maintained at \(800 \mathrm{~K}\) and is located \(0.5 \mathrm{~m}\) from the gage. The surroundings and the air are at \(27^{\circ} \mathrm{C}\) and the convection heat transfer coefficient between the gage and the air is \(15 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). (a) Determine the net radiation exchange between the heater and the gage. (b) Determine the net transfer of radiation to the gage per unit area of the gage. (c) What is the net heat transfer rate to the gage per unit area of the gage? (d) If the gage is constructed according to the description of Problem 3.107, what heat flux will it indicate?

At the bottom of a very large vacuum chamber whose walls are at \(300 \mathrm{~K}\), a black panel \(0.1 \mathrm{~m}\) in diameter is maintained at \(77 \mathrm{~K}\). To reduce the heat gain to this panel, a radiation shield of the same diameter \(D\) and an emissivity of \(0.05\) is placed very close to the panel. Calculate the net heat gain to the panel.

A flue gas at 1 -atm total pressure and a temperature of \(1400 \mathrm{~K}\) contains \(\mathrm{CO}_{2}\) and water vapor at partial pressures of \(0.05\) and \(0.10 \mathrm{~atm}\), respectively. If the gas flows through a long flue of \(1-\mathrm{m}\) diameter and \(400 \mathrm{~K}\) surface temperature, determine the net radiative heat flux from the gas to the surface. Blackbody behavior may be assumed for the surface.

The bottom of a steam-producing still of 200 -mm diameter is heated by radiation. The heater, maintained at \(1000^{\circ} \mathrm{C}\) and separated \(100 \mathrm{~mm}\) from the still, has the same diameter as the still bottom. The still bottom and heater surfaces are black. (a) By what factor could the vapor production rate be increased if the cylindrical sades (dashed sarface) were insulated rather than open to the surroundings maintained at \(27^{\circ} \mathrm{C}\) ? (b) For heater temperatures of 600,800 , and \(1000^{\circ} \mathrm{C}\), plot the net rate of radiation heat transfer to the still as a function of the separation distance over the range from 25 to \(100 \mathrm{~mm}\). Consider the cylindrical sides to be insulated and all other conditions to remain the same.

An electrically heated sample is maintained at a surface temperature of \(T_{s}=500 \mathrm{~K}\). The sample coating is diffuse but spectrally selective, with the spectral emissivity distribution shown schematically. The sample is irradiated by a furnace located coaxially at a distance of \(L_{\mathrm{s}}=750 \mathrm{~mm}\). The furnace has isothermal walls with an emissivity of \(s_{f}=0.7\) and a uniform temperature of \(T_{f}-3000 \mathrm{~K}\). A radiation detector of area \(A_{d}=8 \times 10^{-5} \mathrm{~m}^{2}\) is positioned at a distance of \(L_{\mathrm{dd}}=1.0 \mathrm{~m}\) from the sample along a direction that is \(45^{\circ}\) from the sample normal. The detector is sensitive to spectral radiant power only in the spectral region from 3 to \(5 \mu \mathrm{m}\). The sample surface experiences convection with a gas for which \(T_{\infty}=300 \mathrm{~K}\) and \(h=20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The surroundings of the sample mount are large and at a uniform temperature of \(T_{\text {sur }}=300 \mathrm{~K}\). (a) Determine the electrical power, \(P_{c}\), required to maintain the sample at \(T_{s}=500 \mathrm{~K}\). (b) Considering both emission and reflected irradiation from the sample, determine the radiant power that is incident on the detector within the spectral region from 3 to \(5 \mu \mathrm{m}\).

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