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Copper balls $\left(\rho=8933 \mathrm{~kg} / \mathrm{m}^{3}, \quad k=401 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right.\(, \)c_{p}=385 \mathrm{~J} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}, \alpha=1.166 \times 10^{-4} \mathrm{~m}^{2} / \mathrm{s}\( ) initially at \)180^{\circ} \mathrm{C}$ are allowed to cool in air at \(30^{\circ} \mathrm{C}\) for a period of $2 \mathrm{~min}\(. If the balls have a diameter of \)2 \mathrm{~cm}$ and the heat transfer coefficient is \(80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), the center temperature of the balls at the end of cooling is (a) \(78^{\circ} \mathrm{C}\) (b) \(95^{\circ} \mathrm{C}\) (c) \(118^{\circ} \mathrm{C}\) (d) \(134^{\circ} \mathrm{C}\) (e) \(151^{\circ} \mathrm{C}\)

Short Answer

Expert verified
Answer: The center temperature of the copper balls after cooling for 2 minutes is approximately \(95^\circ\,\text{C}\).

Step by step solution

01

Write down the given information

We are given the following information: - Density of copper, \(\rho = 8933\,\text{kg}/\text{m}^3\) - Thermal conductivity of copper, \(k = 401\,\text{W}/\text{m}\cdot\text{K}\) - Specific heat at constant pressure, \(c_p = 385\,\text{J}/\text{kg}\cdot{ }^\circ\text{C}\) - Heat transfer coefficient, \(h = 80\,\text{W}/\text{m}^2\cdot\text{K}\) - Initial temperature, \(T_1 = 180^\circ\,\text{C}\) - Air temperature, \(T_\infty = 30^\circ\,\text{C}\) - Cooling time, \(t = 2\,\text{min}\) - Diameter of copper balls, \(d = 2 \,\text{cm}\)
02

Apply the Lumped Capacitance method

First we need to calculate the Biot number of the copper balls to determine if the lumped capacitance method is appropriate. Biot number, \(Bi = \frac{hL}{k}\), where L is the characteristic dimension of the geometry (radius in this case). $$L = \frac{d}{2} = \frac{2\,\text{cm}}{2} = 1\,\text{cm} = 0.01\,\text{m}$$ $$Bi = \frac{hL}{k} = \frac{80\,\text{W}/\text{m}^2\cdot\text{K} \cdot 0.01\,\text{m}}{401\,\text{W}/\text{m}\cdot\text{K}} \approx 0.02$$ Since \(Bi < 0.1\), the lumped capacitance method can be applied.
03

Calculate the final temperature

Using the lumped capacitance method, we can now calculate the final center temperature \(T\) of the copper balls by applying Newton's law of cooling: $$T = T_\infty + (T_1 - T_\infty) e^{-\frac{h A}{\rho V c_p}t}$$ - Surface area, \(A = 4\pi r^2 = 4\pi (0.01\,\text{m})^2 \approx 1.2566 \times 10^{-3}\,\text{m}^2\) - Volume, \(V = \frac{4}{3}\pi r^3 = \frac{4}{3}\pi (0.01\,\text{m})^3 \approx 4.1888 \times 10^{-6}\,\text{m}^3\) Now, plug in the values and calculate the final temperature. $$T \approx 30^\circ\,\text{C} + (180^\circ\,\text{C} - 30^\circ\,\text{C})e^{-\frac{80\,\text{W}/\text{m}^2\cdot\text{K} \cdot 1.2566 \times 10^{-3}\,\text{m}^2}{8933\,\text{kg}/\text{m}^3 \cdot 4.1888 \times 10^{-6}\,\text{m}^3 \cdot 385\,\text{J}/\text{kg}\cdot{ }^\circ\text{C} \cdot 120\,\text{s}}} \approx 95^\circ\,\text{C}$$ Thus, the center temperature of the copper balls at the end of cooling is about \(95^\circ\,\text{C}\), which corresponds to option (b).

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Most popular questions from this chapter

A steel casting cools to 90 percent of the original temperature difference in \(30 \mathrm{~min}\) in still air. The time it takes to cool this same casting to 90 percent of the original temperature difference in a moving air stream whose convective heat transfer coefficient is 5 times that of still air is (a) \(3 \mathrm{~min}\) (b) \(6 \mathrm{~min}\) (c) \(9 \mathrm{~min}\) (d) \(12 \mathrm{~min}\) (e) \(15 \mathrm{~min}\)

In a production facility, 3-cm-thick large brass plates $\left(k=110 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \rho=8530 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=380 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right.$, and \(\alpha=33.9 \times\) \(10^{-6} \mathrm{~m}^{2} / \mathrm{s}\) ) that are initially at a uniform temperature of \(25^{\circ} \mathrm{C}\) are heated by passing them through an oven maintained at \(700^{\circ} \mathrm{C}\). The plates remain in the oven for a period of \(10 \mathrm{~min}\). Taking the convection heat transfer coefficient to be $h=80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, determine the surface temperature of the plates when they come out of the oven. Solve this problem using the analytical one-term approximation method. Can this problem be solved using lumped system analysis? Justify your answer.

A thick wood slab \((k=0.17 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and \(\alpha=1.28 \times\) \(10^{-7} \mathrm{~m}^{2} / \mathrm{s}\) ) that is initially at a uniform temperature of \(25^{\circ} \mathrm{C}\) is exposed to hot gases at \(550^{\circ} \mathrm{C}\) for a period of \(5 \mathrm{~min}\). The heat transfer coefficient between the gases and the wood slab is $35 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. If the ignition temperature of the wood is \(450^{\circ} \mathrm{C}\), determine if the wood will ignite.

Stainless steel ball bearings $\left(\rho=8085 \mathrm{~kg} / \mathrm{m}^{3}\right.\(, \)k=15.1 \mathrm{~W} / \mathrm{m} \cdot{ }^{\circ} \mathrm{C}, \quad c_{p}=0.480 \mathrm{KJ} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}, \quad\( and \)\quad \alpha=3.91 \times\( \)10^{-6} \mathrm{~m}^{2} / \mathrm{s}\( ) having a diameter of \)1.2 \mathrm{~cm}$ are to be quenched in water. The balls leave the oven at a uniform temperature of $900^{\circ} \mathrm{C}\( and are exposed to air at \)30^{\circ} \mathrm{C}$ for a while before they are dropped into the water. If the temperature of the balls is not to fall below \(850^{\circ} \mathrm{C}\) prior to quenching and the heat transfer coefficient in the air is $125 \mathrm{~W} / \mathrm{m}^{2},{ }^{\circ} \mathrm{C}$, determine how long they can stand in the air before being dropped into the water.

How does immersion chilling of poultry compare to forced-air chilling with respect to \((a)\) cooling time, \((b)\) moisture loss of poultry, and (c) microbial growth?

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