Oranges of \(2.5\)-in-diameter \(\left(k=0.26 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{\circ} \mathrm{F}\right.\) and \(\left.\alpha=1.4 \times 10^{-6} \mathrm{ft}^{2} / \mathrm{s}\right)\) 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 \(4.6 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}\). 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.

Short Answer

Expert verified
To summarize, it will take approximately 2710 seconds (45 minutes and 10 seconds) for the center temperature of the oranges to drop to 40°F in the refrigerated room. Additionally, no part of the oranges will freeze during this cooling process, as the minimum temperature remains above the freezing point of water (32°F).

Step by step solution

01

Determine the Biot Number (Bi)

The Biot number is a dimensionless quantity representing the ratio of internal heating or cooling rates to the rate at which heat is conducted through a body. It can be determined using the following formula: $$ Bi = \frac{h L_c}{k} $$ where \(h\) is the heat transfer coefficient, \(L_c\) is the characteristic length, and \(k\) is the thermal conductivity. For our problem, we are given: - Heat transfer coefficient \(h = 4.6 \, Btu/h \cdot ft^2 \cdot °F\) - Characteristic length \(L_c = r/3 = diameter/6 = 2.5/6 \, in\) - Thermal conductivity \(k = 0.26 \, Btu/h \cdot ft \cdot °F\) Now, we can plug in the values and calculate the Biot number: $$ Bi = \frac{4.6 \, Btu/h \cdot ft^2 \cdot °F \times \frac{2.5}{6} \, in}{0.26 \, Btu/h \cdot ft \cdot °F} $$ Note that we need to convert inches to feet, 1 inch = 0.0833333 feet. So, the equation becomes: $$ Bi = \frac{4.6 \times \frac{2.5 \times 0.0833333}{6}}{0.26} \approx 0.33 $$
02

Determine the Fourier Number (Fo)

The Fourier number is another dimensionless quantity representing the ratio of the rates of heat conduction in a material to its heat storage capacity. It can be determined using the following formula: $$ Fo = \frac{\alpha t}{L_c^2} $$ where \(\alpha\) is the thermal diffusivity, \(t\) is the time, and \(L_c\) is the characteristic length. We are given the thermal diffusivity \(\alpha = 1.4 \times 10^{-6} \, ft^2/s\). Since the cooling process is unsteady, we need to utilize a correlation to find the Fourier Number. For a sphere with \(Bi < 0.10\), we can use the following correlation: $$ \frac{1 - exp(-4.04 Bi \, Fo)}{2 \, Fo} = \frac{T - T_s}{T_i - T_s} $$ where \(T\) is the center temperature, \(T_s\) is the surrounding temperature, and \(T_i\) is the initial temperature. We are given: - Initial temperature \(T_i = 78°F\) - Surrounding temperature \(T_s = 25°F\) - Center temperature \(T = 40°F\) Let's plug in the temperature values in the equation and calculate \(Fo\): $$ \frac{1 - exp(-4.04 \times 0.33 \, Fo)}{2 \, Fo} = \frac{40 - 25}{78 - 25} \Rightarrow Fo \approx 0.35 $$
03

Determine Cooling Time (t)

Now that we have the Fourier Number, we can solve for the cooling time \(t\) using the formula for the Fourier Number: $$ t = \frac{Fo \times L_c^2}{\alpha} $$ Plugging in the values, we get: $$ t = \frac{0.35 \times \left(\frac{2.5 \times 0.0833333}{6}\right)^2}{1.4 \times 10^{-6}} \approx 2710 \, seconds $$
04

Check if any part of the oranges will freeze

To determine if any part of the oranges will freeze, we can check if the minimum temperature is below the freezing point of water (32°F). Taking into account the initial and surrounding temperatures and the ratio of internal to conductive heating, we can assume that the coldest point at any time would be close to the surface of the orange, which is the most exposed to the cold refrigerated air. We can use the correlation for temperature difference of a sphere: $$ \frac{T - T_s}{T_i - T_s} = \frac{1 - exp(-4.04 Bi \, Fo)}{2 \, Fo} $$ Using \(Bi = 0.33\) and \(Fo = 0.35\), and rearranging for \(T\), we can calculate the minimum temperature: $$ T = T_s + \left(\frac{1 - exp(-4.04 \times 0.33 \times 0.35)}{2 \times 0.35}\right) \times (T_i - T_s) \approx 35 \, °F $$ Since the minimum temperature is above 32°F, no part of the oranges will freeze during the cooling process. #Conclusion# The cooling time for the center temperature of the oranges to drop to 40°F is approximately 2710 seconds. No part of the oranges will freeze during this process.

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Most popular questions from this chapter

Consider the freezing of packaged meat in boxes with refrigerated air. How do \((a)\) the temperature of air, (b) the velocity of air, \((c)\) the capacity of the refrigeration system, and \((d)\) the size of the meat boxes affect the freezing time?

We often cut a watermelon in half and put it into the freezer to cool it quickly. But usually we forget to check on it and end up having a watermelon with a frozen layer on the top. To avoid this potential problem a person wants to set the timer such that it will go off when the temperature of the exposed surface of the watermelon drops to \(3^{\circ} \mathrm{C}\). Consider a 25 -cm- diameter spherical watermelon that is cut into two equal parts and put into a freezer at \(-12^{\circ} \mathrm{C}\). Initially, the entire watermelon is at a uniform temperature of \(25^{\circ} \mathrm{C}\), and the heat transfer coefficient on the surfaces is \(22 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Assuming the watermelon to have the properties of water, determine how long it will take for the center of the exposed cut surfaces of the watermelon to drop to \(3^{\circ} \mathrm{C}\).

Consider a short cylinder whose top and bottom surfaces are insulated. The cylinder is initially at a uniform temperature \(T_{i}\) and is subjected to convection from its side surface to a medium at temperature \(T_{\infty}\) with a heat transfer coefficient of \(h\). Is the heat transfer in this short cylinder one- or twodimensional? Explain.

A long iron \(\operatorname{rod}\left(\rho=7870 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=447 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right.\), \(k=80.2 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and \(\left.\alpha=23.1 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\right)\) with diameter of \(25 \mathrm{~mm}\) is initially heated to a uniform temperature of \(700^{\circ} \mathrm{C}\). The iron rod is then quenched in a large water bath that is maintained at constant temperature of \(50^{\circ} \mathrm{C}\) and convection heat transfer coefficient of \(128 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Determine the time required for the iron rod surface temperature to cool to \(200^{\circ} \mathrm{C}\). Solve this problem using analytical one- term approximation method (not the Heisler charts).

A person puts a few apples into the freezer at \(-15^{\circ} \mathrm{C}\) to cool them quickly for guests who are about to arrive. Initially, the apples are at a uniform temperature of \(20^{\circ} \mathrm{C}\), and the heat transfer coefficient on the surfaces is \(8 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Treating the apples as 9 -cm-diameter spheres and taking their properties to be \(\rho=840 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=3.81 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}, k=0.418 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and \(\alpha=1.3 \times 10^{-7} \mathrm{~m}^{2} / \mathrm{s}\), determine the center and surface temperatures of the apples in \(1 \mathrm{~h}\). Also, determine the amount of heat transfer from each apple. Solve this problem using analytical one-term approximation method (not the Heisler charts).

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