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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.

Short Answer

Expert verified
Answer: It takes 4.46 seconds for the stainless steel ball bearings to cool down from 900°C to 850°C.

Step by step solution

01

Calculate surface area and volume of ball bearings

First, we'll need to calculate the surface area and volume of the stainless steel ball bearing to later calculate the heat transfer. The formula for surface area (A) of a sphere is \(A = 4 \pi r^2\), and the formula for the volume (V) of a sphere is \(V = \frac{4}{3} \pi r^3\) , where r is the radius of the sphere. Given the diameter of the ball bearing is \(1.2 \thinspace cm\), we can calculate the radius as: \(r = \frac{1.2}{2} = 0.6 \thinspace cm = 0.006 \thinspace m\) Now, we can calculate the surface area and volume as: \(A = 4 \pi (0.006)^2 = 4.52 \times 10^{-4} \thinspace m^2\) \(V = \frac{4}{3} \pi (0.006)^3 = 9.05 \times 10^{-7} \thinspace m^3\)
02

Set up the heat transfer equation

Next, we'll set up the heat transfer equation to calculate the heat transfer rate: \(q = hA(T - T_\infty)\) Where \(q\) is the heat transfer rate, \(h\) is the heat transfer coefficient, \(A\) is the surface area, \(T\) is the temperature of the ball bearing, \(T_\infty\) is the surrounding temperature. Given: \(h = 125 \thinspace W/m^2 K\) \(T = 900^\circ C\) \(T_\infty = 30^\circ C\) Now, we can substitute the values into the heat transfer equation: \(q = 125 \times 4.52 \times 10^{-4} (900 - 30) = 39.35 \thinspace W\)
03

Calculate the heat loss required to drop the temperature

To find the heat loss required to drop the temperature from \(900^\circ C\) to \(850^\circ C\), we will use the formula: \(Q = mc_p\Delta{T}\) Where \(Q\) is the heat loss, \(m\) is the mass of the ball bearing, \(c_p\) is the specific heat capacity at constant pressure, and \(\Delta{T}\) is the change in temperature. Given: \(\rho = 8085 \thinspace kg/m^3\) \(c_p = 0.480 \thinspace kJ/kg \cdot ^{\circ}C = 480 \thinspace J/kg \cdot ^{\circ}C\) (converting from kJ to J) \(\Delta{T} = 50^\circ C\) First, we need to calculate the mass of the ball bearing using density: \(m = \rho V = 8085 \times 9.05 \times 10^{-7} = 0.00732 \thinspace kg\) Now, we substitute the values into the heat loss formula: \(Q = 0.00732 \times 480 \times 50 = 175.6 \thinspace J\)
04

Calculate the time required for the temperature to drop

Now that we have the heat transfer rate and the heat loss required to drop the temperature, we can calculate the time required for the temperature drop using: \(t = \frac{Q}{q} = \frac{175.6 \thinspace J}{39.35 \thinspace W} = 4.46 \thinspace s\) So, the stainless steel ball bearings can stand in the air for 4.46 seconds before they need to be dropped into the water to maintain a temperature above \(850^\circ C\).

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Most popular questions from this chapter

What is a semi-infinite medium? Give examples of solid bodies that can be treated as semi-infinite media for heat transfer purposes.

During a picnic on a hot summer day, the only available drinks were those at the ambient temperature of \(90^{\circ} \mathrm{F}\). In an effort to cool a 12 -fluid-oz drink in a can, which is 5 in high and has a diameter of $2.5 \mathrm{in}$, a person grabs the can and starts shaking it in the iced water of the chest at \(32^{\circ} \mathrm{F}\). The temperature of the drink can be assumed to be uniform at all times, and the heat transfer coefficient between the iced water and the aluminum can is $30 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}$. Using the properties of water for the drink, estimate how long it will take for the canned drink to cool to \(40^{\circ} \mathrm{F}\). Solve this problem using lumped system analysis. Is the lumped system analysis applicable to this problem? Why?

Citrus fruits are very susceptible to cold weather, and extended exposure to subfreezing temperatures can destroy them. Consider an 8 -cm-diameter orange that is initially at \(15^{\circ} \mathrm{C}\). A cold front moves in one night, and the ambient temperature suddenly drops to \(-6^{\circ} \mathrm{C}\), with a heat transfer coefficient of $15 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Using the properties of water for the orange and assuming the ambient conditions remain constant for \(4 \mathrm{~h}\) before the cold front moves out, determine if any part of the orange will freeze that night. Solve this problem using the analytical one-term approximation method.

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: \(486^{\circ} \mathrm{C}, 22,270 \mathrm{~kJ}\)

Oranges of \(2.5\)-in-diameter $\left(k=0.26 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}\right.\( and \)\alpha=1.4 \times 10^{-6} \mathrm{ft}^{2} / \mathrm{s}$ ) initially at a uniform temperature of \(78^{\circ} \mathrm{F}\) are to be cooled by refrigerated air at $25^{\circ} \mathrm{F}\( flowing at a velocity of \)1 \mathrm{ft} / \mathrm{s}$. The average heat transfer coefficient between the oranges and the air is experimentally determined to be $4.6 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}$. Determine how long it will take for the center temperature of the oranges to drop to \(40^{\circ} \mathrm{F}\). Also, determine if any part of the oranges will freeze during this process. Solve this problem using the analytical one-term approximation method.

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