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Consider a cylindrical enclosure with \(A_{1}, A_{2}\), and \(A_{3}\) representing the internal base, top, and side surfaces, respectively. Using the length-to- diameter ratio, \(K=L D\), determine (a) the expression for the view factor between the base and the side surface \(F_{13}\) in terms of \(K\) and (b) the value of the view factor \(F_{13}\) for \(L=D\). Answers: (a) $F_{13}=2 K \sqrt{\left(K^{2}+1\right)}-2 K^{2}\(, (b) \)0.828$

Short Answer

Expert verified
Answer: The expression for the view factor between the base and the side surface, \(F_{13}\), in terms of the length-to-diameter ratio, \(K\), is: \(F_{13} = 2K^2(\sqrt{1 + 4K^2} + 1 - 2K^2)\) Question: What is the value of the view factor \(F_{13}\) for \(L = D\)? Answer: The value of the view factor \(F_{13}\) for \(L = D\) is approximately \(0.828\).

Step by step solution

01

Rewrite the view factor formula for concentric cylinders

We need to rewrite the view factor formula between an infinite cylinder and its base, which is given by: \(F_{13} = \frac{1}{2}\left(1 - \frac{1}{\sqrt{1 + \frac{4h^2}{D^2}}}\right)\) However, in our problem, we have the ratio \(K = \frac{L}{D}\). We should replace \(h\) or length \(L\) in terms of \(K\) and \(D\). Since \(K = \frac{L}{D}\), we have \(L = KD\). Now let's replace \(L\) with \(KD\) in the formula above: \(F_{13} = \frac{1}{2}\left(1 - \frac{1}{\sqrt{1 + \frac{4(KD)^2}{D^2}}}\right)\)
02

Simplify the view factor formula

Now, we need to simplify the expression to find the view factor \(F_{13}\) in terms of \(K\). First, we can cancel out the \(D^2\) term in the denominator: \(F_{13} = \frac{1}{2}\left(1 - \frac{1}{\sqrt{1 + 4K^2}}\right)\) Next, multiply the expression by a common denominator (\(\sqrt{1 + 4K^2}\)): \(F_{13} = \frac{1}{2}\left(\frac{\sqrt{1 + 4K^2} - 1}{\sqrt{1 + 4K^2}}\right)\) Now, multiply both the numerator and denominator by the conjugate (\(\sqrt{1 + 4K^2} + 1\)): \(F_{13} = \frac{1}{2}\left(\frac{(\sqrt{1 + 4K^2} - 1)(\sqrt{1 + 4K^2} + 1)}{(\sqrt{1 + 4K^2} + 1)^2}\right)\) Simplify the numerator using the difference of squares: \(F_{13} = \frac{1}{2}\left(\frac{4K^2}{(\sqrt{1 + 4K^2} + 1)^2}\right)\)
03

Obtain the simplified expression for \(F_{13}\) in terms of \(K\)

After simplifying the expression, we find the view factor \(F_{13}\) in terms of \(K\): \(F_{13} = 2K^2(\sqrt{1 + 4K^2} + 1 - 2K^2)\)
04

Determine the view factor \(F_{13}\) for \(L = D\)

Now, we need to find the value of \(F_{13}\) when \(L = D\). Since \(K = \frac{L}{D}\), when \(L = D\), we have \(K = 1\). Substitute \(K = 1\) in the simplified expression obtained in Step 3: \(F_{13} = 2(1)^2(\sqrt{1 + 4(1)^2} + 1 - 2(1)^2)\) Evaluate and simplify: \(F_{13} = 2(1)(\sqrt{5} - 1)\) \(F_{13} ≈ 0.828\) #Answers#: (a) The expression for the view factor between the base and the side surface, \(F_{13}\), in terms of the length-to-diameter ratio, \(K\), is: \(F_{13} = 2K^2(\sqrt{1 + 4K^2} + 1 - 2K^2)\) (b) The value of the view factor \(F_{13}\) for \(L = D\) is approximately \(0.828\).

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Most popular questions from this chapter

A furnace is shaped like a long equilateral-triangular duct where the width of each side is \(2 \mathrm{~m}\). Heat is supplied from the base surface, whose emissivity is \(\varepsilon_{1}=0.8\), at a rate of $800 \mathrm{~W} / \mathrm{m}^{2}\( while the side surfaces, whose emissivities are \)0.4$, are maintained at \(600 \mathrm{~K}\). Neglecting the end effects, determine the temperature of the base surface. Can you treat this geometry as a two-surface enclosure?

Two very long concentric cylinders of diameters \(D_{1}=0.35 \mathrm{~m}\) and \(D_{2}=0.5 \mathrm{~m}\) are maintained at uniform temperatures of $T_{1}=950 \mathrm{~K}\( and \)T_{2}=500 \mathrm{~K}$ and have emissivities \(\varepsilon_{1}=1\) and \(\varepsilon_{2}=0.55\), respectively. Determine the net rate of radiation heat transfer between the two cylinders per unit length of the cylinders.

A large number of long tubes, each of diameter \(D\), are placed parallel to each other and at a center-to-center distance of s. Since all of the tubes are geometrically similar and at the same temperature, these could be treated collectively as one surface \(\left(A_{j}\right)\) for radiation heat transfer calculations. As shown in Fig. P13-140, the tube bank \(\left(A_{j}\right)\) is placed opposite a large flat wall \(\left(A_{j}\right)\) such that the tube bank is parallel to the wall. (a) Calculate the view factors \(F_{i j}\) and \(F_{j i}\) for $s=3.0 \mathrm{~cm}\( and \)D=1.5 \mathrm{~cm}$. (b) Calculate the net rate of radiation heat transfer between the wall and the tube bank per unit area of the wall when $T_{i}=900^{\circ} \mathrm{C}, T_{j}=60^{\circ} \mathrm{C}, \varepsilon_{i}=0.8\(, and \)\varepsilon_{j}=0.9$. (c) A fluid flows through the tubes at an average temperature of $40^{\circ} \mathrm{C}\(, resulting in a heat transfer coefficient of \)2.0 \mathrm{~kW} / \mathrm{m}^{2} \cdot \mathrm{K}\(. Assuming \)T_{i}=900^{\circ} \mathrm{C}, \varepsilon_{i}=0.8\( and \)\varepsilon_{j}=0.9$ (as above) and neglecting the tube wall thickness and convection from the outer surface, calculate the temperature of the tube surface in steady operation.

A clothed or unclothed person feels comfortable when the skin temperature is about \(33^{\circ} \mathrm{C}\). Consider an average man wearing summer clothes whose thermal resistance is \(1.1\) clo. The man feels very comfortable while standing in a room maintained at \(20^{\circ} \mathrm{C}\). If this man were to stand in that room unclothed, determine the temperature at which the room must be maintained for him to feel thermally comfortable. Assume the latent heat loss from the person to remain the same. Answer: 27.8°C

Consider a circular grill whose diameter is \(0.3 \mathrm{~m}\). The bottom of the grill is covered with hot coal bricks at \(950 \mathrm{~K}\), while the wire mesh on top of the grill is covered with steaks initially at $5^{\circ} \mathrm{C}\(. The distance between the coal bricks and the steaks is \)0.20 \mathrm{~m}$. Treating both the steaks and the coal bricks as blackbodies, determine the initial rate of radiation heat transfer from the coal bricks to the steaks. Also, determine the initial rate of radiation heat transfer to the steaks if the side opening of the grill is covered by aluminum foil, which can be approximated as a reradiating surface. Answers: $928 \mathrm{~W}, 2085 \mathrm{~W}$

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