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A short brass cylinder $\left(\rho=8530 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=0.389 \mathrm{~kJ} /\right.\( \)\mathrm{kg} \cdot \mathrm{K}, k=110 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(, and \)\left.\alpha=3.39 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\right)\( of diameter \)4 \mathrm{~cm}$ and height \(20 \mathrm{~cm}\) is initially at a uniform temperature of $150^{\circ} \mathrm{C}\(. The cylinder is now placed in atmospheric air at \)20^{\circ} \mathrm{C}$, where heat transfer takes place by convection with a heat transfer coefficient of \(40 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Calculate \((a)\) the center temperature of the cylinder; \((b)\) the center temperature of the top surface of the cylinder; and (c) the total heat transfer from the cylinder \(15 \mathrm{~min}\) after the start of the cooling. Solve this problem using the analytical one-term approximation method.

Short Answer

Expert verified
Question: After 15 minutes of cooling, determine the following for a short brass cylinder: (a) the center temperature of the cylinder, (b) the center temperature of the top surface, and (c) the total heat transfer from the cylinder. Answer: (a) The center temperature of the cylinder is \(68.75^\circ\text{C}\), (b) the center temperature of the top surface is \(59.45^\circ\text{C}\), and (c) the total heat transfer from the cylinder after 15 minutes is 54230.93 J.

Step by step solution

01

Compute the Biot number (Bi)

The Biot number is given by the formula: Bi = \(hL_c/k\) Where \(h\) is the heat transfer coefficient, \(L_c\) is the characteristic length of the cylinder, and \(k\) is the thermal conductivity. The characteristic length of a solid cylinder is given by \(L_c = V/A\), where \(V\) is the volume, and \(A\) is the surface area. For a short cylinder, the height is much greater than the diameter so we can use the height as the characteristic length, \(L_c = 20 \times 10^{-2}\text{ m}\). Now, we can compute the Biot number: Bi = \((40\text{ W/m}^2\text{K}) \cdot (20 \times 10^{-2}\text{ m}) / (110\text{ W/mK})\) Bi = 0.0727
02

Calculate the Fourier number (Fo)

The Fourier number is given by the formula: Fo = \(\alpha t / L_c^2\) Where \(\alpha\) is the thermal diffusivity, \(t\) is time, and \(L_c\) is the characteristic length. We are given \(\alpha = 3.39 \times 10^{-5}\text{ m}^2/\text{s}\), and the cooling time \(t = 15\text{ min} = 900\text{ s}\). Now, we can compute the Fourier number: Fo = \((3.39 \times 10^{-5}\text{ m}^2/\text{s})\cdot (900\text{ s}) / (20 \times 10^{-2}\text{ m})^2\) Fo = 0.00759
03

Determine the temperature ratio (TR)

using the Bi and Fo values, we can look up the one-term approximation value from the analytical solution of transient conduction in a solid cylinder. For Bi = 0.0727 and Fo = 0.00759, the temperature ratio TR = 0.375
04

Calculate the center temperature (a) and the center temperature of the top surface (b) using the temperature ratio (TR)

We know the initial temperature \(T_i = 150^\circ\text{C}\) and the air temperature \(T_\infty = 20^\circ\text{C}\). We can calculate the temperatures using the formula: \(T(x,t) = T_\text{A} + (T_\text{B} - T_\text{A})\text{TR}\) (a) For the center temperature of the cylinder: \(T_\text{center} = 20 + (150 - 20)(0.375)\) \(T_\text{center} = 68.75^\circ\text{C}\) (b) For the center temperature of the top surface of the cylinder, we have Bi/2 instead of Bi in the TR formula. Thus, we find a new TR value for the top surface temperature ratio. For Bi/2 = 0.0727/2 and Fo = 0.00759, we find that TR = 0.303 \(T_\text{top surface} = 20 + (150 - 20)(0.303)\) \(T_\text{top surface} = 59.45^\circ\text{C}\)
05

Calculate the total heat transfer (c) from the cylinder

Find q/Q from the table for Bi = 0.0727 and Fo = 0.00759: q/Q = 0.507 The total heat stored in the body at the beginning is given by: \(Q = mc_\text{p} (T_i - T_\infty)\) We need to compute the mass \(m\) of the cylinder: \(m = V \rho\). The volume of the cylinder \(V = \pi r^2 h = \pi (0.02\text{ m})^2 (0.2\text{ m})\). Using the given density \(\rho = 8530\text{ kg/m}^3\), we can compute the mass: \(m = (\pi (0.02\text{ m})^2 (0.2\text{ m}))(8530\text{ kg/m}^3) = 1.713\text{ kg}\) Now, we can calculate the initial heat stored in the cylinder: \(Q = (1.713\text{ kg}) \cdot (390\text{ J/kgK}) \cdot (150 - 20)\) \(Q = 106978.1\text{ J}\) Finally, we can calculate the total heat transfer from the cylinder after 15 minutes: \(q = Q \cdot \text{(q/Q)}\) \(q = 106978.1 \cdot 0.507\) \(q = 54230.93\text{ J}\) Therefore, (a) the center temperature of the cylinder is \(68.75^\circ\text{C}\), (b) the center temperature of the top surface is \(59.45^\circ\text{C}\), and (c) the total heat transfer from the cylinder after 15 minutes is 54230.93 J.

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Most popular questions from this chapter

The temperature of a gas stream is to be measured by a thermocouple whose junction can be approximated as a \(1.2\)-mm-diameter sphere. The properties of the junction are $k=35 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \rho=8500 \mathrm{~kg} / \mathrm{m}^{3}\(, and \)c_{p}=320 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$, and the heat transfer coefficient between the junction and the gas is \(h=110 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Determine how long it will take for the thermocouple to read 99 percent of the initial temperature difference.

The Biot number during a heat transfer process between a sphere and its surroundings is determined to be \(0.02\). Would you use lumped system analysis or the one-term approximate solutions when determining the midpoint temperature of the sphere? Why?

Thick slabs of stainless steel $(k=14.9 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\( and \)\left.\alpha=3.95 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\right)\( and copper \)(k=401 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\( and \)\left.\alpha=117 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\right)$ are placed under an array of laser diodes, which supply an energy pulse of \(5 \times 10^{7} \mathrm{~J} / \mathrm{m}^{2}\) instantaneously at \(t=0\) to both materials. The two slabs have a uniform initial temperature of \(20^{\circ} \mathrm{C}\). Determine the temperatures of both slabs at $5 \mathrm{~cm}\( from the surface and \)60 \mathrm{~s}$ after receiving an energy pulse from the laser diodes.

A long 35-cm-diameter cylindrical shaft made of stainless steel $304\left(k=14.9 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \rho=7900 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=477 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right.\(, and \)\alpha=3.95 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\( ) comes out of an oven at a uniform temperature of \)500^{\circ} \mathrm{C}$. The shaft is then allowed to cool slowly in a chamber at \(150^{\circ} \mathrm{C}\) with an average convection heat transfer coefficient of \(h=60 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Determine the temperature at the center of the shaft 20 min after the start of the cooling process. Also, determine the heat transfer per unit length of the shaft during this time period. Solve this problem using the analytical one-term approximation method. Answers: \(486^{\circ} \mathrm{C}, 22,270 \mathrm{~kJ}\)

How can we use the one-term approximate solutions when the surface temperature of the geometry is specified instead of the temperature of the surrounding medium and the convection heat transfer coefficient?

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