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A hot surface at \(100^{\circ} \mathrm{C}\) is to be cooled by attaching 3 -cm- long, \(0.25\)-cm-diameter aluminum pin fins \((k=237\) $\mathrm{W} / \mathrm{m} \cdot \mathrm{K})\( to it, with a center-to-center distance of \)0.6 \mathrm{~cm}\(. The temperature of the surrounding medium is \)30^{\circ} \mathrm{C}\(, and the heat transfer coefficient on the surfaces is \)35 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Determine the rate of heat transfer from the surface for a \(1-\mathrm{m} \times 1-\mathrm{m}\) section of the plate. Also determine the overall effectiveness of the fins.

Short Answer

Expert verified
Answer: The rate of heat transfer from the 1 m x 1 m finned surface is 83,141.10 W and the overall effectiveness of the pin fins is 33.79.

Step by step solution

01

Calculate the number of fins on the plate

To determine the number of fins on the 1 m x 1 m plate, we will first find the number of fins in one row and column and then find the total number of fins. The center-to-center distance between the fins is 0.6 cm, so we will first convert it to meters. Number of fins per row = Length of the plate (in meters)/ Center-to-center distance (in meters) = 1/0.006 = 166.67 ~ 167 fins Number of fins per column = Width of the plate (in meters)/ Center-to-center distance (in meters) = 1/0.006 = 166.67 ~ 167 fins Total number of fins on the plate = Number of fins per row × Number of fins per column = 167 × 167 = 27889 fins
02

Calculate the fin's efficiency

To calculate the fin's efficiency, we will first need to calculate the fin parameter \(m\), length of the fin \(L\), and the circumference of the fin \(P\). Fin parameter \(m = \sqrt{\frac{hP}{kA_c}}\), where \(h\) is the heat transfer coefficient, \(P\) is the circumference of fin, \(k\) is the thermal conductivity of the material, and \(A_c\) is the cross-sectional area of the fin. \(L = 3 \times 10^{-2} m\), Diameter \(D = 0.25 \times 10^{-2} m\), \(A_c = \pi\frac{D^2}{4} = \pi\frac{(0.25 \times 10^{-2})^2}{4}\), \(P = \pi D = \pi(0.25 \times 10^{-2})\) \(h=35 \mathrm{~W} / \mathrm{m}^2 \cdot \mathrm{K}\) and \(k=237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) Fin parameter \(m = \sqrt{\frac{35\pi(0.25 \times 10^{-2})}{237\pi\frac{(0.25 \times 10^{-2})^2}{4}}} = 24.34\) \(m^{-1}\) Fin efficiency \(\eta_{fin} = \frac{\tanh{(\frac{mLhP}{kA_c})}}{\frac{mLhP}{kA_c}}= \frac{\tanh{(24.34 \times 0.03)}}{24.34 \times 0.03} = 0.952\)
03

Calculate the rate of heat transfer from the finned surface

The heat transfer rate of one fin, \(q_f\) is given by the formula, \(q_f = \eta_{fin} h A_f (T_b - T_{ambient})\). \(A_f\) is the fin's heat-transfer area, \(A_f = PL\). Using the fin efficiency \(\eta_{fin}=0.952\), heat transfer coefficient \(h = 35\) W/m²K, \(A_f = \pi(0.25 \times 10^{-2}) \times 0.03\), base temperature \(T_b = 100 ^\circ \mathrm{C}\) and ambient temperature, \(T_{ambient} = 30 ^\circ \mathrm{C}\), we can find the rate of heat transfer from one fin: \(q_f = 0.952\times 35 \times \pi(0.25 \times 10^{-2}) \times 0.03 \times (100-30) = 2.980\) \(\mathrm{W}\) Total heat transfer rate from the surface with fins, \(q_t = q_f \times N\), where \(N\) is the total number of fins. \(q_t = 2.980 \times 27889 = 83141.10\) \(\mathrm{W}\)
04

Calculate the overall effectiveness of the fins

The overall effectiveness of the fins can be calculated using the formula, \(\eta_o = \frac{q_t}{q_{max}}\), where \(q_{max}\) is the maximum heat transfer rate, which would occur without fins. \(q_{max} = h A_{unfinned} (T_b - T_{ambient})\), \(A_{unfinned}\) is the unfinned area of the plate \(A_{unfinned} = A_{plate} - N \times A_c = 1 \times 1 - 27889 \times \pi\frac{(0.25 \times 10^{-2})^2}{4} = 0.942\) \(m^2\) \(q_{max} = 35 \times 0.942 \times (100 - 30) = 2459.10\) \(\mathrm{W}\) Overall effectiveness of the fins, \(\eta_o = \frac{83141.10}{2459.10} = 33.79\) So the rate of heat transfer from the surface for a 1 m x 1 m section of the plate is \(83141.10\) \(\mathrm{W}\) and the overall effectiveness of the fins is \(33.79\).

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Most popular questions from this chapter

Two plate fins of constant rectangular cross section are identical, except that the thickness of one of them is twice the thickness of the other. For which fin is the \((a)\) fin effectiveness and (b) fin efficiency higher? Explain.

Hot water flows in a 1-m-long section of a pipe that is made of acrylonitrile butadiene styrene (ABS) thermoplastic. The \(\mathrm{ABS}\) pipe section has an inner diameter of \(D_{1}=22 \mathrm{~mm}\) and an outer diameter of $D_{2}=27 \mathrm{~mm}\(. The thermal conductivity of the ABS pipe wall is \)0.1 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. The outer pipe surface is exposed to convection heat transfer with air at \(20^{\circ} \mathrm{C}\) and $h=10 \mathrm{~W} / \mathrm{m}^{2} . \mathrm{K}$. The water flowing inside the pipe has a convection heat transfer coefficient of $50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. According to the ASME Code for Process Piping (ASME B31.3-2014, Table B-1), the maximum recommended temperature for \(\mathrm{ABS}\) pipe is \(80^{\circ} \mathrm{C}\). Determine the maximum temperature of the water flowing in the pipe, such that the ABS pipe is operating at the recommended temperature or lower. What is the temperature at the outer pipe surface when the water is at maximum temperature?

A 12 -m-long and 8-cm-diameter hot-water pipe of a district heating system is buried in the soil \(80 \mathrm{~cm}\) below the ground surface. The outer surface temperature of the pipe is \(60^{\circ} \mathrm{C}\). Taking the surface temperature of the earth to be \(2^{\circ} \mathrm{C}\) and the thermal conductivity of the soil at that location to be $0.9 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$, determine the rate of heat loss from the pipe.

Circular cooling fins of diameter \(D=1 \mathrm{~mm}\) and length $L=30 \mathrm{~mm}\(, made of copper \)(k=380 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$, are used to enhance heat transfer from a surface that is maintained at temperature \(T_{s 1}=132^{\circ} \mathrm{C}\). Each rod has one end attached to this surface \((x=0)\), while the opposite end \((x=L)\) is joined to a second surface, which is maintained at \(T_{s 2}=0^{\circ} \mathrm{C}\). The air flowing between the surfaces and the rods is also at \(T_{\infty}=0^{\circ} \mathrm{C}\). and the convection coefficient is $h=100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. (a) Express the function \(\theta(x)=T(x)-T_{\infty}\) along a fin, and calculate the temperature at \(x=L / 2\). (b) Determine the rate of heat transferred from the hot surface through each fin and the fin effectiveness. Is the use of fins justified? Why? (c) What is the total rate of heat transfer from a \(10-\mathrm{cm}\) by \(10-\mathrm{cm}\) section of the wall, which has 625 uniformly distributed fins? Assume the same convection coefficient for the fin and for the unfinned wall surface.

Obtain a relation for the fin efficiency for a fin of constant cross-sectional area \(A_{c}\), perimeter \(p\), length \(L\), and thermal conductivity \(k\) exposed to convection to a medium at \(T_{\infty}\) with a heat transfer coefficient \(h\). Assume the fins are sufficiently long so that the temperature of the fin at the tip is nearly \(T_{\infty}\). Take the temperature of the fin at the base to be \(T_{b}\) and neglect heat transfer from the fin tips. Simplify the relation for \((a)\) a circular fin of diameter \(D\) and \((b)\) rectangular fins of thickness \(t\).

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