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

To warm up some milk for a baby, a mother pours milk into a thin-walled cylindrical container whose diameter is \(6 \mathrm{~cm}\). The height of the milk in the container is \(7 \mathrm{~cm}\). She then places the container into a large pan filled with hot water at \(70^{\circ} \mathrm{C}\). The milk is stirred constantly so that its temperature is uniform at all times. If the heat transfer coefficient between the water and the container is $120 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, determine how long it will take for the milk to warm up from \(3^{\circ} \mathrm{C}\) to $38^{\circ} \mathrm{C}$. Assume the entire surface area of the cylindrical container (including the top and bottom) is in thermal contact with the hot water. Take the properties of the milk to be the same as those of water. Can the milk in this case be treated as a lumped system? Why? Answer: \(4.50\) min

Short Answer

Expert verified
Answer: It takes about 8.86 minutes to heat the milk from 3°C to 38°C, and the milk cannot be treated as a lumped system in this case.

Step by step solution

01

Calculate the volume of the milk

The volume (V) of the cylindrical container filled with milk is given by the formula: $$V = \frac{\pi d^2}{4} \times h$$ Let's convert the diameter and height to meters and then calculate the volume. $$V = \frac{\pi (0.06 \mathrm{~m})^2}{4} \times 0.07 \mathrm{~m} = 0.0001885 \mathrm{~m}^3$$
02

Find the mass of the milk

Using the density of the milk (which is assumed to be the same as water), we can calculate the mass of the milk as follows: $$m = \rho \times V = (1000 \mathrm{~kg} / \mathrm{m}^3) \times 0.0001885 \mathrm{~m}^3 = 0.1885 \mathrm{~kg}$$
03

Calculate the surface area of the container

The surface area (A) of the cylindrical container in contact with the water (including the top and bottom) can be calculated as: $$A = \pi d^2 + 2 \pi \left(\frac{d}{2} \right)h = 2 \pi \left(\frac{d}{2} \right) \times (d + 2h)$$ $$A = 2 \pi \left(0.03 \mathrm{~m} \right) \times (0.06 \mathrm{~m} + 2 \times 0.07 \mathrm{~m}) = 0.02568 \mathrm{~m}^2$$
04

Determine the time required for the milk to reach the final temperature

The total heat (Q) required to raise the milk's temperature from \(T_i\) to \(T_f\) can be calculated using the formula: $$Q = m \times c_p \times \Delta T = m \times c_p \times (T_f - T_i)$$ $$Q = (0.1885 \mathrm{~kg}) \times (4186 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}) \times (38 - 3)^{\circ} \mathrm{C} = 27438 \mathrm{~J}$$ The heat transfer rate (Q') can be calculated using the formula: $$Q' = h \times A \times (T_w - T_m)$$ Here, \(T_w\) is the temperature of the water and \(T_m\) is the average temperature of the milk. We will take \(T_m\) as the midpoint of \(T_i\) and \(T_f\). $$Q' = (120 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}) \times 0.02568 \mathrm{~m}^2 \times (70 - \frac{3 + 38}{2})^{\circ} \mathrm{C} = 51.61 \mathrm{~W}$$ Now, we can find the time (t) required for the milk to reach the final temperature: $$t = \frac{Q}{Q'} = \frac{27438 \mathrm{~J}}{51.61 \mathrm{~W}} = 531.48 \mathrm{~s}$$ $$t = 531.48 \mathrm{~s} = 8.86 \mathrm{~min}$$
05

Check if the milk can be treated as a lumped system

To check if the milk can be treated as a lumped system, we calculate the Biot number (Bi): $$Bi = \frac{hL_c}{k}$$ Here, \(L_c\) is the characteristic length, which can be calculated as: $$L_c = \frac{V}{A}$$ $$L_c = \frac{0.0001885 \mathrm{~m}^3}{0.02568 \mathrm{~m}^2} = 0.007339\ \mathrm{m}$$ Now, we calculate the Biot number: $$Bi = \frac{(120 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}) \times 0.007339 \mathrm{~m}}{0.6 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}} = 1.467$$ Since the Biot number \(Bi > 0.1\), the milk cannot be treated as a lumped system. In conclusion, it takes about 8.86 minutes to heat the milk from \(3^{\circ} \mathrm{C}\) to \(38^{\circ} \mathrm{C}\) and the milk cannot be treated as a lumped system in this case.

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

A thermocouple with a spherical junction diameter of \(0.5 \mathrm{~mm}\) is used for measuring the temperature of hot airflow in a circular duct. The convection heat transfer coefficient of the airflow can be related with the diameter \((D)\) of the spherical junction and the average airflow velocity \((V)\) as \(h=2.2(V / D)^{0.5}\), where \(D, h\), and \(V\) are in $\mathrm{m}, \mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}\(, and \)\mathrm{m} / \mathrm{s}$, respectively. The properties of the thermocouple junction are $k=35 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(, \)\rho=8500 \mathrm{~kg} / \mathrm{m}^{3}\(, and \)c_{p}=320 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$. Determine the minimum airflow velocity that the thermocouple can use, if the maximum response time of the thermocouple to register 99 percent of the initial temperature difference is \(5 \mathrm{~s}\).

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.

A heated 6-mm-thick Pyroceram plate $\left(\rho=2600 \mathrm{~kg} / \mathrm{m}^{3}\right.\(, \)c_{p}=808 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}, k=3.98 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(, and \)\left.\alpha=1.89 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\right)$ is being cooled in a room with air temperature of \(25^{\circ} \mathrm{C}\) and convection heat transfer coefficient of \(13.3 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The heated Pyroceram plate had an initial temperature of \(500^{\circ} \mathrm{C}\), and it is allowed to cool for \(286 \mathrm{~s}\). If the mass of the Pyroceram plate is \(10 \mathrm{~kg}\), determine the heat transfer from the Pyroceram plate during the cooling process using the analytical one-term approximation method.

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.

Long cylindrical AISI stainless steel rods $\left(k=7.74 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{\circ} \mathrm{F}\right.$ and \(\left.\alpha=0.135 \mathrm{ft}^{2} / \mathrm{h}\right)\) of 4 -in diameter are heat treated by drawing them at a velocity of \(7 \mathrm{ft} / \mathrm{min}\) through a 21 -ft-long oven maintained at \(1700^{\circ} \mathrm{F}\). The heat transfer coefficient in the oven is $20 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}$. If the rods enter the oven at \(70^{\circ} \mathrm{F}\), determine their centerline temperature when they leave. Solve this problem using the analytical one-term approximation method.

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