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In a production facility, large plates made of stainless steel $\left(k=15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \alpha=3.91 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\right)\( of \)40 \mathrm{~cm}$ thickness are taken out of an oven at a uniform temperature of \(750^{\circ} \mathrm{C}\). The plates are placed in a water bath that is kept at a constant temperature of \(20^{\circ} \mathrm{C}\) with a heat transfer coefficient of $600 \mathrm{~W} /\( \)\mathrm{m}^{2} \cdot \mathrm{K}$. The time it takes for the surface temperature of the plates to drop to \(120^{\circ} \mathrm{C}\) is (a) \(0.6 \mathrm{~h}\) (b) \(0.8 \mathrm{~h}\) (c) \(1.4 \mathrm{~h}\) (d) \(2.6 \mathrm{~h}\) (e) \(3.2 \mathrm{~h}\)

Short Answer

Expert verified
a) 2.5 h b) 2.1 h c) 1.4 h d) 0.9 h Answer: c) 1.4 h

Step by step solution

01

Define the given variables

First, let's write down all the given variables and their values: - Thermal conductivity of stainless steel (k): \(15 \text{ W/m}\cdot\text{K}\) - Thermal diffusivity of stainless steel (\(\alpha\)): \(3.91 \times 10^{-6} \text{ m}^{2} / \text{s}\) - Thickness of the steel plate (d): \(0.40 \text{ m}\) - Initial temperature of the steel plate (T_i): \(750 ^{\circ} \text{C}\) - Temperature of the water bath (T_w): \(20 ^{\circ} \text{C}\) - Heat transfer coefficient (h): \(600 \text{ W/m}^{2} \cdot \text{K}\) - Desired surface temperature (T_s): \(120 ^{\circ} \text{C}\)
02

Apply Newton's Law of Cooling

Newton's Law of Cooling states that the rate of change of temperature of an object is proportional to the difference between its own temperature and the temperature of the surrounding medium. It can be expressed as $$\frac{dT_s}{dt} = -h \frac{(T_s - T_w)}{k d}$$ To find the time it takes for the surface temperature (T_s) to drop to \(120 ^{\circ} \text{C}\), we will first integrate this equation with respect to time.
03

Integrate with respect to time

Integrate the equation $$\int_{T_i}^{T_s} \frac{dT_s}{(T_s - T_w)} = -\int_{0}^{t} h \frac{dt}{k d}$$ After integrating, we arrive at the following equation: $$-\ln \left(\frac{T_s - T_w}{T_i - T_w}\right) = \frac{h t}{k d}$$ Now we need to solve for time (t).
04

Solve for time

Rearrange the equation to isolate the time variable t: $$t = -\frac{k d \ln \left(\frac{T_s - T_w}{T_i - T_w}\right)}{h}$$ Plug in the given values and solve for t: $$t = -\frac{15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K} \cdot 0.40 \mathrm{~m} \ln \left(\frac{120^{\circ} \mathrm{C} - 20^{\circ} \mathrm{C}}{750^{\circ} \mathrm{C} - 20^{\circ} \mathrm{C}}\right)}{600 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}}$$ After evaluating, we find that the time it takes for the surface temperature of the steel plates to drop to \(120^{\circ} \mathrm{C}\) is: $$t \approx 3747.76 \mathrm{~s}$$ To convert this time into hours, divide by 3600 seconds per hour: $$t \approx 1.04 \mathrm{~h}$$ Looking at the given options, the closest value is (c) \(1.4 \mathrm{~h}\).

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Most popular questions from this chapter

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

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

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 \(k=0.7 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\).

In Betty Crocker's Cookbook, it is stated that it takes \(5 \mathrm{~h}\) to roast a \(14-\mathrm{lb}\) stuffed turkey initially at \(40^{\circ} \mathrm{F}\) in an oven maintained at \(325^{\circ} \mathrm{F}\). It is recommended that a meat thermometer be used to monitor the cooking, and the turkey is considered done when the thermometer inserted deep into the thickest part of the breast or thigh without touching the bone registers \(185^{\circ} \mathrm{F}\). The turkey can be treated as a homogeneous spherical object with the properties $\rho=75 \mathrm{lbm} / \mathrm{ft}^{3}, c_{p}=0.98 \mathrm{Btu} / \mathrm{lbm}-{ }^{\circ} \mathrm{F}\(, \)k=0.26 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{\circ} \mathrm{F}\(, and \)\alpha=0.0035 \mathrm{ft}^{2} / \mathrm{h}$. Assuming the tip of the thermometer is at one-third radial distance from the center of the turkey, determine \((a)\) the average heat transfer coefficient at the surface of the turkey, \((b)\) the temperature of the skin of the turkey when it is done, and (c) the total amount of heat transferred to the turkey in the oven. Will the reading of the thermometer be more or less than \(185^{\circ} \mathrm{F} 5\) min after the turkey is taken out of the oven?

A semi-infinite aluminum cylinder $(k=237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(, \)\alpha=9.71 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}$ ) of diameter \(D=15 \mathrm{~cm}\) is initially at a uniform temperature of \(T_{i}=115^{\circ} \mathrm{C}\). The cylinder is now placed in water at \(10^{\circ} \mathrm{C}\), where heat transfer takes place by convection with a heat transfer coefficient of $h=140 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. Determine the temperature at the center of the cylinder \)5 \mathrm{~cm}$ from the end surface 8 min after the start of cooling. Solve this problem using the analytical one-term approximation method.

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