Warning: foreach() argument must be of type array|object, bool given in /var/www/html/web/app/themes/studypress-core-theme/template-parts/header/mobile-offcanvas.php on line 20

After a long, hard week on the books, you and your friend are ready to relax and enjoy the weekend. You take a steak \(50 \mathrm{~mm}\) thick from the freezer. (a) How long (in hours) do you have to let the good times roll before the steak has thawed? Assume that the steak is initially at $-8^{\circ} \mathrm{C}$, that it thaws when the temperature at the center of the steak reaches \(4^{\circ} \mathrm{C}\), and that the room temperature is $22^{\circ} \mathrm{C}\( with a convection heat transfer coefficient of \)10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Neglect the heat of fusion associated with the melting phase change. Treat the steak as a one-dimensional plane wall having the following properties: \(\rho=1000 \mathrm{~kg} / \mathrm{m}^{3}\), \(c_{p}=4472 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\), and $k=0.625 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. (b) How much energy per unit area (in J/m²) has been removed from the steak during this period of thawing? (c) Show whether or not the thawing of this steak can be analyzed by neglecting the internal thermal resistance of the steak.

Short Answer

Expert verified
2. How long does it take for the steak to thaw, in hours? 3. What is the energy per unit area removed from the steak during the thawing period? 4. Can the internal thermal resistance of the steak be neglected in this problem?

Step by step solution

01

Find the temperature difference

First, we need to find the difference in temperature between the center of the steak and the room. The center of the steak goes from -8°C to 4°C, and the room is at 22°C. The temperature difference is: \(\Delta T = T_{room} - T_{center} = 22^{\circ} \mathrm{C} - 4^{\circ} \mathrm{C} = 18^{\circ} \mathrm{C}\).
02

Calculate the thawing time

Next, we will use the convection heat transfer formula to find the thawing time, which is given by: \(t = \frac{\rho h c_p}{k} \frac{\Delta T}{h_c}\) Here, \(h = 0.05 \mathrm{~m}\) (thickness of the steak), \(h_c = 10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (convection heat transfer coefficient), and the steak's properties are given. Plugging in the values, we get: \(t = \frac{1000 \mathrm{~kg} / \mathrm{m}^{3} \cdot 0.05\mathrm{~m} \cdot 4472 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}}{0.625 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}} \cdot \frac{18^{\circ} \mathrm{C}}{10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}}\) \(t = 673.44 \mathrm{~s}\). Since we need to find the time in hours, we will convert as follows: \(t_{hours} = \frac{673.44 \mathrm{~s}}{3600 \mathrm{~s/hour}} = 0.1871 \mathrm{~hours}\).
03

Calculate the energy per unit area removed from the steak

Since we know the thawing time, we can now calculate the total energy lost per unit area during this period of thawing using the following equation: \(Q = h_c \cdot \Delta T \cdot t\) So, \(Q = 10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K} \times 18^{\circ} \mathrm{C} \times 673.44 \mathrm{~s}\) \(Q = 121184 \mathrm{~J/m^2}\).
04

Analyze the internal thermal resistance of the steak

The internal thermal resistance can be determined by analyzing the Biot number, which is a dimensionless number that represents the ratio of internal resistance to surface resistance. It is given by: \(Bi = \frac{h L}{k}\) , where \(L\) is the characteristic length of the steak (in our case, L=h). If \(Bi < 0.1\), it is considered that the internal thermal resistance is negligible. Let's calculate the Biot number for the given steak: \(Bi = \frac{10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K} \cdot 0.05 \mathrm{~m}}{0.625 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}}\) \(Bi = 0.8\) Since \(Bi > 0.1\), we can conclude that the internal thermal resistance of the steak cannot be neglected in this problem. In summary, the time it takes for the steak to thaw is approximately 0.19 hours, the energy per unit area removed from the steak during this period of thawing is 121,184 J/m², and the internal thermal resistance of the steak cannot be neglected in this analysis.

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

Carbon steel balls $\left(\rho=7833 \mathrm{~kg} / \mathrm{m}^{3}, k=54 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right.\(, \)c_{p}=0.465 \mathrm{~kJ} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}\(, and \)\left.\alpha=1.474 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\right) 8 \mathrm{~mm}$ in diameter are annealed by heating them first to \(900^{\circ} \mathrm{C}\) in a furnace and then allowing them to cool slowly to \(100^{\circ} \mathrm{C}\) in ambient air at \(35^{\circ} \mathrm{C}\). If the average heat transfer coefficient is $75 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, determine how long the annealing process will take. If 2500 balls are to be annealed per hour, determine the total rate of heat transfer from the balls to the ambient air.

Spherical glass beads coming out of a kiln are allowed to cool in a room temperature of \(30^{\circ} \mathrm{C}\). A glass bead with a diameter of $10 \mathrm{~mm}\( and an initial temperature of \)400^{\circ} \mathrm{C}$ is allowed to cool for \(3 \mathrm{~min}\). If the convection heat transfer coefficient is \(28 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine the temperature at the center of the glass bead using the analytical one-term approximation method. The glass bead has properties of $\rho=2800 \mathrm{~kg} / \mathrm{m}^{3}\(, \)c_{p}=750 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$, and \(k=0.7 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\).

A large chunk of tissue at \(35^{\circ} \mathrm{C}\) with a thermal diffusivity of \(1 \times 10^{-7} \mathrm{~m}^{2} / \mathrm{s}\) is dropped into iced water. The water is well-stirred so that the surface temperature of the tissue drops to \(0^{\circ} \mathrm{C}\) at time zero and remains at \(0^{\circ} \mathrm{C}\) at all times. The temperature of the tissue after 4 min at a depth of $1 \mathrm{~cm}$ is (a) \(5^{\circ} \mathrm{C}\) (b) \(30^{\circ} \mathrm{C}\) (c) \(25^{\circ} \mathrm{C}\) (d) \(20^{\circ} \mathrm{C}\) (e) \(10^{\circ} \mathrm{C}\)

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?

An electronic device dissipating \(18 \mathrm{~W}\) has a mass of $20 \mathrm{~g}\(, a specific heat of \)850 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\(, and a surface area of \)4 \mathrm{~cm}^{2}$. The device is lightly used, and it is on for \(5 \mathrm{~min}\) and then off for several hours, during which it cools to the ambient temperature of \(25^{\circ} \mathrm{C}\). Taking the heat transfer coefficient to be $12 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, determine the temperature of the device at the end of the 5-min operating period. What would your answer be if the device were attached to an aluminum heat sink having a mass of \(200 \mathrm{~g}\) and a surface area of \(80 \mathrm{~cm}^{2}\) ? Assume the device and the heat sink to be nearly isothermal.

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free