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Layers of \(23-\mathrm{cm}\)-thick meat slabs $(k=0.47 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\( and \)\alpha=0.13 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\( ) initially at a uniform temperature of \)7^{\circ} \mathrm{C}$ are to be frozen by refrigerated air at \(-30^{\circ} \mathrm{C}\) flowing at a velocity of \(1.4 \mathrm{~m} / \mathrm{s}\). The average heat transfer coefficient between the meat and the air is $20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Assuming the size of the meat slabs to be large relative to their thickness, determine how long it will take for the center temperature of the slabs to drop to \(-18^{\circ} \mathrm{C}\). Also, determine the surface temperature of the meat slab at that time.

Short Answer

Expert verified
Question: Determine the time it takes for a meat slab at an initial temperature of \(7^{\circ} \mathrm{C}\) to be frozen such that the temperature at the center becomes \(-18^{\circ} \mathrm{C}\), and calculate the surface temperature of the meat slab at that time.

Step by step solution

01

Determine if the lumped capacitance method is applicable

To determine the applicability of the lumped capacitance method, we need to calculate the Biot number: $$\mathrm{Bi} = \frac{hL_c}{k}$$ Where \(h\) is the heat transfer coefficient, \(L_c\) is the characteristic length, and \(k\) is the thermal conductivity. For a slab with a thickness of \(23 \mathrm{~cm}\), the characteristic length is equal to half the thickness: $$L_c = \frac{23}{2} \times 10^{-2} \mathrm{~m}$$ Now, let's calculate the Biot number: $$\mathrm{Bi} = \frac{20 \mathrm{~W} \cdot \mathrm{m}^{-2} \cdot \mathrm{K}^{-1}(11.5 \times 10^{-2} \mathrm{~m})}{0.47 \mathrm{~W} \cdot \mathrm{m}^{-1} \cdot \mathrm{K}^{-1}}$$ If the Biot number is less than 0.1, the lumped capacitance method can be applied.
02

Calculate the time required for the center temperature to drop to \(-18^{\circ} \mathrm{C}\)

Using the lumped capacitance method, the following formula relates the temperature at any time \(t\): $$\theta(t) = \theta_i - (\theta_i - \theta_\infty)(1 - e^{-t \frac{hA_s}{V\rho c})})$$ Here, \(\theta(t)\) is the temperature at time \(t\), \(\theta_i\) is the initial temperature, \(\theta_\infty\) is the surrounding temperature, and \(A_s\) is the surface area. From the given information, we know that the initial temperature (\(\theta_i\)) is \(7^{\circ} \mathrm{C}\) and the surrounding temperature (\(\theta_\infty\)) is \(-30^{\circ} \mathrm{C}\). We want to calculate the time it takes for the temperature at the center to be \(-18^{\circ} \mathrm{C}\). Hence, let \(\theta(t) = -18^{\circ} \mathrm{C}\), and we can solve for \(t\): $$-18 = 7 - (7 - (-30))(1 - e^{-t\frac{20A_s}{V\rho c)})$$ The surface area, \(A_s\), for a slab with a large area relative to its thickness can be considered as the area of one side. Assume \(1 \mathrm{~m}^2\) for simplicity: $$A_s = 1 \mathrm{~m}^2$$ We know that \(\rho = \frac{1}{\alpha}\) and since \(\alpha = 0.13 \times 10^{-6} \mathrm{~m}^{2} \cdot \mathrm{s}^{-1}\): $$\rho = \frac{1}{0.13 \times 10^{-6}}$$ Assuming constant volume, we can write the volume \(V\) as: $$V = A_s L_c$$ Since we have already calculated \(L_c\) in Step 1, substitute that value, and now we have all the necessary information to find the time, \(t\).
03

Calculate the surface temperature of the meat slab at that time

Once we have calculated the time \(t\), we can use the lumped capacitance method formula again to find the surface temperature at that time. In this case, we'll use the parameter \(x = 0\) to represent the surface temperature. The formula becomes: $$\theta_s(t) = \theta_i - (\theta_i - \theta_\infty)(1 - e^{-t\frac{hA_s}{V\rho c}})$$ Simply substitute the values for \(\theta_i\), \(\theta_\infty\), \(h\), \(A_s\), \(V\), \(\rho\), and \(c\) along with the time \(t\) we found in Step 2 to calculate the surface temperature of the meat slab at that time.

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Most popular questions from this chapter

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.

The chilling room of a meat plant is \(15 \mathrm{~m} \times\) $18 \mathrm{~m} \times 5.5 \mathrm{~m}$ in size and has a capacity of 350 beef carcasses. The power consumed by the fans and the lights in the chilling room are 22 and $2 \mathrm{~kW}$, respectively, and the room gains heat through its envelope at a rate of \(14 \mathrm{~kW}\). The average mass of beef carcasses is $220 \mathrm{~kg}\(. The carcasses enter the chilling room at \)35^{\circ} \mathrm{C}$, after they are washed to facilitate evaporative cooling, and are cooled to \(16^{\circ} \mathrm{C}\) in \(12 \mathrm{~h}\). The air enters the chilling room at \(-2.2^{\circ} \mathrm{C}\) and leaves at $0.5^{\circ} \mathrm{C}\(. Determine \)(a)$ the refrigeration load of the chilling room and \((b)\) the volume flow rate of air. The average specific heats of beef carcasses and air are \(3.14\) and $1.0 \mathrm{~kJ} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}$, respectively, and the density of air can be taken to be \(1.28 \mathrm{~kg} / \mathrm{m}^{3}\).

A barefooted person whose feet are at \(32^{\circ} \mathrm{C}\) steps on a large aluminum block at \(20^{\circ} \mathrm{C}\). Treating both the feet and the aluminum block as semi-infinite solids, determine the contact surface temperature. What would your answer be if the person stepped on a wood block instead? At room temperature, the \(\sqrt{k \rho c_{p}}\) value is $24 \mathrm{~kJ} / \mathrm{m}^{2},{ }^{\circ} \mathrm{C}\( for aluminum, \)0.38 \mathrm{~kJ} / \mathrm{m}^{2},{ }^{\circ} \mathrm{C}\( for wood, and \)1.1 \mathrm{~kJ} / \mathrm{m}^{2},{ }^{\circ} \mathrm{C}$ for human flesh.

Carbon steel balls $\left(\rho=7830 \mathrm{~kg} / \mathrm{m}^{3}, k=64 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right.\(, \)\left.c_{p}=434 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( initially at \)200^{\circ} \mathrm{C}\( are quenched in an oil bath at \)20^{\circ} \mathrm{C}$ for a period of \(3 \mathrm{~min}\). If the balls have a diameter of \(5 \mathrm{~cm}\) and the convection heat transfer coefficient is $450 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, the center temperature of the balls after quenching will be (Hint: Check the Biot number.) (a) \(30.3^{\circ} \mathrm{C}\) (b) \(46.1^{\circ} \mathrm{C}\) (c) \(55.4^{\circ} \mathrm{C}\) (d) \(68.9^{\circ} \mathrm{C}\) (e) \(79.4^{\circ} \mathrm{C}\)

A steel casting cools to 90 percent of the original temperature difference in \(30 \mathrm{~min}\) in still air. The time it takes to cool this same casting to 90 percent of the original temperature difference in a moving air stream whose convective heat transfer coefficient is 5 times that of still air is (a) \(3 \mathrm{~min}\) (b) \(6 \mathrm{~min}\) (c) \(9 \mathrm{~min}\) (d) \(12 \mathrm{~min}\) (e) \(15 \mathrm{~min}\)

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