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Steel rods, \(2 \mathrm{~m}\) in length and \(60 \mathrm{~mm}\) in diameter, are being drawn through an oven that maintains a temperature of $800^{\circ} \mathrm{C}\( and convection heat transfer coefficient of \)128 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. The steel rods \)\left(\rho=7832 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=434 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}, k=63.9\right.\( \)\mathrm{W} / \mathrm{m} \cdot \mathrm{K}\(, and \)\alpha=18.8 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}$ ) were initially in uniform temperature of \(30^{\circ} \mathrm{C}\). Using the analytical one-term approximation method, determine the amount of heat transferred to the steel rod after \(133 \mathrm{~s}\) of heating.

Short Answer

Expert verified
Question: Determine the amount of heat transferred to a steel rod after being heated for 133 seconds in an oven. Answer: The amount of heat transferred to the steel rod after 133 seconds of heating is 20,874 W.

Step by step solution

01

Analyze the necessary formulas

The following formula will be used to estimate the heat transfer per length, obtained from the analytical one-term approximation method: \(q_{L}=\frac{k}{r} q_{1}\left[1-e^{-n_{1}^{2} \frac{\alpha t}{r^{2}}}\right]\). In this formula, \(q_{L}\) is the heat transfer per unit length. \(k\) is the thermal conductivity of the steel. \(r\) is the radius of the steel rod. \(q_{1}\) is the first Fourier sine series coefficient. \(n_{l}\) is the first non-dimensional eigenvalue. \(t\) is the time of heating. \(\alpha\) is the thermal diffusivity of the steel.
02

Calculate values for constants

We can find the values for the given parameters first. Given the diameter of the steel rod, we can find its radius as: \(r = \frac{60}{2}\times 10^{-3}\,\mathrm{m} = 0.03\,\mathrm{m}\). As per the one-term approximation method, we have \(n_{1} = \frac{2}{\pi}\) and \(q_{1} = \frac{2Nu_{\infty}\delta}{\pi}\), where \(Nu_{\infty}\) is the Nusselt number in a fully developed Biot number asymptotic limit and \(\delta\) is the difference in temperature between the oven and the initial rod temperature \(=800^{\circ}\mathrm{C} - 30^{\circ}\mathrm{C} = 770\,\mathrm{K}\). Using the given convection heat transfer coefficient, \(h = 128\,\mathrm{W}/\mathrm{m}^2\cdot\,\mathrm{K}\), we can find the Nusselt number as \(Nu_{\infty} = \frac{hr}{k} = \frac{128\times0.03}{63.9} = 0.06\). Finally, we have the values for all the constants in the formula.
03

Calculate the heat transfer per length after 133 seconds

We can now substitute all the values into the formula to find the heat transfer per length after \(133\,\mathrm{s}\) of heating: \(q_{L}=\frac{63.9}{0.03} \left(\frac{2\times0.06\times770}{\pi}\right)\left[1-\exp\left(-\left(\frac{2}{\pi}\right)^{2} \frac{18.8\times10^{-6}\times133}{(0.03)^2}\right)\right]\). Calculating this, we get \(q_{L}=10437\,\mathrm{W}/\mathrm{m}\).
04

Calculate the total heat transferred after 133 seconds

Now that we have found the heat transfer per length, we can multiply it by the total length of the rod to find the total heat transferred. Total heat transferred \((Q) = q_{L}\times\mathrm{Length} = 10437\,\mathrm{W}/\mathrm{m}\times2\,\mathrm{m} = 20874\,\mathrm{W}\). Thus, the amount of heat transferred to the steel rod after \(133\,\mathrm{s}\) of heating is \(20874\,\mathrm{W}\).

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Most popular questions from this chapter

Polyvinylchloride automotive body panels \((k=0.092\) $\left.\mathrm{W} / \mathrm{m} \cdot \mathrm{K}, c_{p}=1.05 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}, \rho=1714 \mathrm{~kg} / \mathrm{m}^{3}\right), 1 \mathrm{~mm}$ thick, emerge from an injection molder at \(120^{\circ} \mathrm{C}\). They need to be cooled to \(40^{\circ} \mathrm{C}\) by exposing both sides of the panels to \(20^{\circ} \mathrm{C}\) air before they can be handled. If the convective heat transfer coefficient is $15 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$ and radiation is not considered, the time that the panels must be exposed to air before they can be handled is (a) \(0.8 \mathrm{~min}\) (b) \(1.6 \mathrm{~min}\) (c) \(2.4 \mathrm{~min}\) (d) \(3.1 \mathrm{~min}\) (e) \(5.6 \mathrm{~min}\)

What is the proper storage temperature of frozen poultry? What are the primary methods of freezing for poultry?

A large ASTM A203 B steel plate, with a thickness of \(7 \mathrm{~cm}\), in a cryogenic process is suddenly exposed to very cold fluid at $-50^{\circ} \mathrm{C}\( with \)h=594 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. The plate has a thermal conductivity of $52 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(, a specific heat of \)470 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\(, and a density of \)7.9 \mathrm{~g} / \mathrm{cm}^{3}$. The ASME Code for Process Piping limits the minimum suitable temperature for ASTM A203 B steel plate to \(-30^{\circ} \mathrm{C}\) (ASME B31.32014 , Table A-1M). If the initial temperature of the plate is \(20^{\circ} \mathrm{C}\) and the plate is exposed to the cryogenic fluid for \(6 \mathrm{~min}\), would it still comply with the ASME code?

The chilling room of a meat plant is \(15 \mathrm{~m} \times\) $18 \mathrm{~m} \times 5.5 \mathrm{~m}$ in size and has a capacity of 350 beef carcasses. The power consumed by the fans and the lights in the chilling room are 22 and $2 \mathrm{~kW}$, respectively, and the room gains heat through its envelope at a rate of \(14 \mathrm{~kW}\). The average mass of beef carcasses is $220 \mathrm{~kg}\(. The carcasses enter the chilling room at \)35^{\circ} \mathrm{C}$, after they are washed to facilitate evaporative cooling, and are cooled to \(16^{\circ} \mathrm{C}\) in \(12 \mathrm{~h}\). The air enters the chilling room at \(-2.2^{\circ} \mathrm{C}\) and leaves at $0.5^{\circ} \mathrm{C}\(. Determine \)(a)$ the refrigeration load of the chilling room and \((b)\) the volume flow rate of air. The average specific heats of beef carcasses and air are \(3.14\) and $1.0 \mathrm{~kJ} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}$, respectively, and the density of air can be taken to be \(1.28 \mathrm{~kg} / \mathrm{m}^{3}\).

Long aluminum wires of diameter $3 \mathrm{~mm}\left(\rho=2702 \mathrm{~kg} / \mathrm{m}^{3}\right.\(, \)c_{p}=0.896 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}, k=236 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$, and \(\left.\alpha=9.75 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\right)\) are extruded at a temperature of \(350^{\circ} \mathrm{C}\) and exposed to atmospheric air at \(30^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(35 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). (a) Determine how long it will take for the wire temperature to drop to \(50^{\circ} \mathrm{C}\). (b) If the wire is extruded at a velocity of 10 \(\mathrm{m} / \mathrm{min}\), determine how far the wire travels after extrusion by the time its temperature drops to \(50^{\circ} \mathrm{C}\). What change in the cooling process would you propose to shorten this distance? (c) Assuming the aluminum wire leaves the extrusion room at $50^{\circ} \mathrm{C}$, determine the rate of heat transfer from the wire to the extrusion room. Answers: (a) \(144 \mathrm{~s}\), (b) \(24 \mathrm{~m}\), (c) $856 \mathrm{~W}$

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