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The walls of a furnace are made of \(1.5\)-ft-thick concrete $\left(k=0.64 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}\right.\( and \)\left.\alpha=0.023 \mathrm{ft}^{2} / \mathrm{h}\right)$. Initially, the furnace and the surrounding air are in thermal equilibrium at \(70^{\circ} \mathrm{F}\). The furnace is then fired, and the inner surfaces of the furnace are subjected to hot gases at $1800^{\circ} \mathrm{F}$ with a very large heat transfer coefficient. Determine how long it will take for the temperature of the outer surface of the furnace walls to rise to \(70.1^{\circ} \mathrm{F}\). Answer: \(3.0 \mathrm{~h}\)

Short Answer

Expert verified
Answer: It will take approximately 3.0 hours for the outer surface temperature of the furnace walls to rise to 70.1°F.

Step by step solution

01

Identify Known Parameters

We start by listing all given parameters: - Concrete thickness: \(L = 1.5 \thinspace ft\) - Thermal conductivity: \(k = 0.64 \thinspace \frac{Btu}{h \cdot ft \cdot ^{\circ}F}\) - Thermal diffusivity: \(\alpha = 0.023 \thinspace \frac{ft^2}{h}\) - Initial temperature: \(T_i = 70^{\circ}F\) - Inner surface temperature after firing: \(T_{1f} = 1800^{\circ}F\) - Desired outer surface temperature: \(T_{2d} = 70.1^{\circ}F\)
02

Calculate Temperature Rise at the Outer Surface

In order to find the time it takes for the outer surface to reach the desired temperature, let's first find the temperature rise at the outer surface of the furnace walls: \(\Delta T = T_{2d} - T_i = 70.1 - 70 = 0.1^{\circ}F\)
03

Use Transient Heat Conduction Formula

Now, we will utilize the transient heat conduction formula for a semi-infinite wall with an initial temperature of \(T_i\) and a constant surface temperature of \(T_{1f}\) at the inner surface. The temperature at a distance \(L\) from the inner surface and after time \(t\) can be given as: $$ T(x=L, t) = T_i + (T_{1f} - T_i)[1 - \mathrm{erf}\left(\frac{L}{2\sqrt{\alpha t}}\right)]$$
04

Solve for the Time

Next, plug the known parameters and the temperature rise at the outer surface into the equation to solve for the time \(t\): $$ T_{2d} = T_i + (T_{1f} - T_i) \left[1 - \mathrm{erf}\left(\frac{L}{2\sqrt{\alpha t}}\right)\right]$$ Substituting the values: $$ 70.1 = 70 + (1800 - 70) \left[1 - \mathrm{erf}\left(\frac{1.5}{2\sqrt{0.023 t}}\right)\right]$$ After rearranging the equation and using a lookup table for the error function, we can find the value of \(t\). Solving for \(t\), we get: $$t \approx 3.0 \thinspace h$$ Thus, it will take about \(3.0\) hours for the temperature of the outer surface of the furnace walls to rise to \(70.1^{\circ}F\).

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Most popular questions from this chapter

During a fire, the trunks of some dry oak trees $\left(k=0.17 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right.\( and \)\left.\alpha=1.28 \times 10^{-7} \mathrm{~m}^{2} / \mathrm{s}\right)$ that are initially at a uniform temperature of \(30^{\circ} \mathrm{C}\) are exposed to hot gases at \(600^{\circ} \mathrm{C}\) for a period of \(4 \mathrm{~h}\), with a heat transfer coefficient of \(65 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) on the surface. The ignition temperature of the trees is \(410^{\circ} \mathrm{C}\). Treating the trunks of the trees as long cylindrical rods of diameter $20 \mathrm{~cm}$, determine if these dry trees will ignite as the fire sweeps through them. Solve this problem using the analytical one-term approximation method.

It is claimed that beef can be stored for up to two years at $-23^{\circ} \mathrm{C}\( but no more than one year at \)-12^{\circ} \mathrm{C}$. Is this claim reasonable? Explain.

What are the environmental factors that affect the growth rate of microorganisms in foods?

A 30-cm-diameter, 4-m-high cylindrical column of a house made of concrete $\left(k=0.79 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \alpha=5.94 \times 10^{-7} \mathrm{~m}^{2} / \mathrm{s}\right.\(, \)\rho=1600 \mathrm{~kg} / \mathrm{m}^{3}\(, and \)c_{p}=0.84 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}$ ) cooled to \(14^{\circ} \mathrm{C}\) during a cold night is heated again during the day by being exposed to ambient air at an average temperature of \(28^{\circ} \mathrm{C}\) with an average heat transfer coefficient of $14 \mathrm{~W} / \mathrm{m}^{2}\(. \)\mathrm{K}$. Using the analytical one-term approximation method, determine \((a)\) how long it will take for the column surface temperature to rise to \(27^{\circ} \mathrm{C}\), (b) the amount of heat transfer until the center temperature reaches to \(28^{\circ} \mathrm{C}\), and \((c)\) the amount of heat transfer until the surface temperature reaches \(27^{\circ} \mathrm{C}\).

A long nickel alloy (ASTM B335) cylindrical rod is used as a component in high-temperature process equipment. The rod has a diameter of $5 \mathrm{~cm}\(; its thermal conductivity, specific heat, and density are \)11 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, 380 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\(, and \)9.3 \mathrm{~g} / \mathrm{cm}^{3}$, respectively. Occasionally, the rod is submerged in hot fluid for several minutes, where the fluid temperature is \(500^{\circ} \mathrm{C}\) with a convection heat transfer coefficient of \(440 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The ASME Code for Process Piping limits the maximum use temperature for ASTM B335 rod to \(427^{\circ} \mathrm{C}\) (ASME B31.32014 , Table A-1M). If the initial temperature of the rod is \(20^{\circ} \mathrm{C}\), how long can the rod be submerged in the hot fluid before reaching its maximum use temperature?

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