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Consider a \(3-\mathrm{m} \times 3-\mathrm{m} \times 3-\mathrm{m}\) cubical furnace. The base surface is black and has a temperature of \(400 \mathrm{~K}\). The radiosities for the top and side surfaces are calculated to be $7500 \mathrm{~W} / \mathrm{m}^{2}\( and \)3200 \mathrm{~W} / \mathrm{m}^{2}$, respectively. If the temperature of the side surfaces is \(485 \mathrm{~K}\), the emissivity of the side surfaces is (a) \(0.37\) (b) \(0.55\) (c) \(0.63\) (d) \(0.80\) (e) \(0.89\)

Short Answer

Expert verified
Answer: (c) 0.63

Step by step solution

01

Identify the given quantities

Given: Base surface temperature, \(T_b=400\:K\) Radiosity for the top surface, \(J_t=7500\:W/m^2\) Radiosity for the side surfaces, \(J_s=3200\:W/m^2\) Temperature of the side surfaces, \(T_s=485\:K\)
02

Write the formula to calculate emissivity

Emissivity (\(\epsilon\)) is given by the formula: \(\epsilon=\frac{J}{\sigma T^4}\) where, \(\sigma\) is the Stefan-Boltzmann constant with a value of \(5.67 \times 10^{-8}\: \text{W}/\text{m}^2\text{K}^4\) \(J\) is the radiosity \(T\) is the temperature Our aim is to determine the emissivity of the side surfaces using the given values.
03

Substitute the given values in the emissivity formula

Now let's substitute the values of \(J_s\), \(\sigma\) and \(T_s\) to find the emissivity of the side surfaces. \(\epsilon=\frac{J_s}{\sigma T_s^4} = \frac{3200}{(5.67 \times 10^{-8})(485)^4}\)
04

Calculate the emissivity

Now calculate the emissivity by using the substituted values in the formula: \(\epsilon \approx \frac{3200}{(5.67 \times 10^{-8})(485)^4} \approx 0.63\) So, the emissivity of the side surfaces is approximately \(0.63\). The correct answer is (c) \(0.63\).

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Most popular questions from this chapter

Two aligned parallel rectangles with dimensions $6 \mathrm{~m} \times 8 \mathrm{~m}\( are spaced apart by a distance of \)2 \mathrm{~m}$. If the two parallel rectangles are experiencing radiation heat transfer as black surfaces, determine the percentage of change in radiation heat transfer rate when the rectangles are moved \(8 \mathrm{~m}\) apart.

A long cylindrical power cable is shielded with placed in parallel with a long cylindrical metal rod that is maintained at a temperature of $150^{\circ} \mathrm{C}$. Both the power cable and the metal rod have the same diameter of \(1 \mathrm{~cm}\), and they are inside a blackbody surrounding at $27^{\circ} \mathrm{C}$. Their distance apart from each other, measured from their centers, is \(20 \mathrm{~cm}\). The emissivity values for the metal rod and the polyethylene insulation are \(0.33\) and 0.95, respectively. According to the ASTM D1351-14 standard specification, the polyethylene insulation is suitable for operation at temperatures up to \(75^{\circ} \mathrm{C}\). If the radiation heat transfer per unit area from the metal rod is $445 \mathrm{~W} / \mathrm{m}^{2}$, determine whether the polyethylene insulation for the power cable would comply with the ASTM D1351-14 standard specification.

Two square plates, with the sides \(a\) and \(b\) (and \(b>a\) ), are coaxial and parallel to each other, as shown in Fig. P13-142, and they are separated by a center-to-center distance of \(L\). The radiation view factor from the smaller to the larger plate, \(F_{a b+}\) is given by $$ F_{a b}=\frac{1}{2 A}\left\\{\left[(B+A)^{2}+4\right]^{0.5}-\left[(B-A)^{2}+4\right]^{0.5}\right\\} $$ where, \(A=a / L\) and \(B=b / L\). (a) Calculate the view factors \(F_{a b}\) and \(F_{b a}\) for $a=20 \mathrm{~cm}\(, \)b=60 \mathrm{~cm}\(, and \)L=40 \mathrm{~cm}$. (b) Calculate the net rate of radiation heat exchange between the two plates described above if \(T_{a}=800^{\circ} \mathrm{C}\), $T_{b}=200^{\circ} \mathrm{C}, \varepsilon_{a}=0.8\(, and \)\varepsilon_{b}=0.4$. (c) A large, square plate (with the side $c=2.0 \mathrm{~m}, \varepsilon_{c}=0.1$, and negligible thickness) is inserted symmetrically between the two plates such that it is parallel to and equidistant from them. For the data given above, calculate the temperature of this third plate when steady operating conditions are established.

A simple solar collector is built by placing a 6-cmdiameter clear plastic tube around a garden hose whose outer diameter is \(2 \mathrm{~cm}\) (Fig. P13-137). The hose is painted black to maximize solar absorption, and some plastic rings are used to keep the spacing between the hose and the clear plastic cover constant. The emissivities of the hose surface and the glass cover are \(0.9\), and the effective sky temperature is estimated to be \(15^{\circ} \mathrm{C}\). The temperature of the plastic tube is measured to be \(40^{\circ} \mathrm{C}\), while the ambient air temperature is \(25^{\circ} \mathrm{C}\). Determine the rate of heat loss from the water in the hose by natural convection and radiation per meter of its length under steady conditions. Answers: $12.7 \mathrm{~W}, 26.1 \mathrm{~W}$

A thin aluminum sheet with an emissivity of \(0.15\) on both sides is placed between two very large parallel plates, which are maintained at uniform temperatures \(T_{1}=900 \mathrm{~K}\) and \(T_{2}=650 \mathrm{~K}\) and have emissivities \(\varepsilon_{1}=0.5\) and \(\varepsilon_{2}=0.8\), respectively. Determine the net rate of radiation heat transfer between the two plates per unit surface area of the plates, and compare the result with that without the shield.

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