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Chickens with an average mass of \(1.7 \mathrm{~kg}(k=0.45\) $\mathrm{W} / \mathrm{m} \cdot \mathrm{K}\( and \)\alpha=0.13 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\( ) initially at a uniform temperature of \)15^{\circ} \mathrm{C}$ are to be chilled in agitated brine at \(-7^{\circ} \mathrm{C}\). The average heat transfer coefficient between the chicken and the brine is determined experimentally to be \(440 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Taking the average density of the chicken to be $0.95 \mathrm{~g} / \mathrm{cm}^{3}$ and treating the chicken as a spherical lump, determine the center and the surface temperatures of the chicken in \(2 \mathrm{~h}\) and $45 \mathrm{~min}$. Also, determine if any part of the chicken will freeze during this process. Solve this problem using the analytical one-term approximation method.

Short Answer

Expert verified
Based on the given problem, calculate the center and surface temperatures of the chicken after being in the brine for 1 hour, and determine if any part of the chicken will freeze during this time.

Step by step solution

01

Calculate the Biot number (Bi) and Fourier number (Fo)

The Biot number is given by the formula: \[Bi = \frac{hR_c}{k}\] and the Fourier number is given by: \[Fo = \frac{\alpha t}{R_c^2}\] where - \(h\) is the heat transfer coefficient (\(440 \mathrm{W/m^2 K}\)) - \(R_c\) is the characteristic radius of the chicken - \(k\) is the thermal conductivity of the chicken (\(0.45 \mathrm{W/mK}\)) - \(\alpha\) is the thermal diffusivity of the chicken (\(0.13 \times 10^{-6} \mathrm{m^2/s}\)) - \(t\) is the time in seconds First, let's find \(R_c\). The volume of a sphere is given by the formula: \[V = \frac{4}{3}\pi R_c^3\] From the given average density and mass of the chicken, we can find the volume: \[V = \frac{m}{\rho} = \frac{1.7 \mathrm{kg}}{0.95 \times 10^3 \mathrm{kg/m^3}}\] Now, we can find \(R_c\) using the volume formula:
02

Calculate the dimensionless temperature

Now we need to calculate the dimensionless temperature using the one-term approximation method: \[Θ^* = \frac{1}{3\sqrt{Bi\cdot Fo}} = \frac{1}{3\sqrt{(hR_ck)\cdot(\frac{\alpha t}{R_c^2})}}\] This will give us the dimensionless temperature at the center of the sphere. Next, let's find the dimensionless temperature at the surface, which is given by \(Θ^*_s = 0\) (since the surface is in contact with the brine at constant temperature).
03

Calculate the actual temperatures at the center and the surface

Now we can find the actual temperatures at the center and the surface of the chicken using the dimensionless temperatures and the formula: \[T = T_\infty + (T_i - T_\infty) Θ^*\] where - \(T_\infty\) is the environmental temperature, which is the brine temperature (\(-7^\circ\mathrm{C}\)) - \(T_i\) is the initial temperature of the chicken (\(15^\circ\mathrm{C}\))
04

Determine if any part of the chicken will freeze

To determine if any part of the chicken will freeze, we need to check if the temperature at any point falls below the freezing point of the chicken (\(0^\circ\mathrm{C}\)). If the center or surface temperature calculated in Step 3 is less than \(0^\circ\mathrm{C}\), then that part of the chicken will freeze. Otherwise, the chicken will not freeze.

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Most popular questions from this chapter

A short brass cylinder $\left(\rho=8530 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=0.389 \mathrm{~kJ} /\right.\( \)\mathrm{kg} \cdot \mathrm{K}, k=110 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(, and \)\left.\alpha=3.39 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\right)\( of diameter \)4 \mathrm{~cm}$ and height \(20 \mathrm{~cm}\) is initially at a uniform temperature of $150^{\circ} \mathrm{C}\(. The cylinder is now placed in atmospheric air at \)20^{\circ} \mathrm{C}$, where heat transfer takes place by convection with a heat transfer coefficient of \(40 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Calculate \((a)\) the center temperature of the cylinder; \((b)\) the center temperature of the top surface of the cylinder; and (c) the total heat transfer from the cylinder \(15 \mathrm{~min}\) after the start of the cooling. Solve this problem using the analytical one-term approximation method.

A large cast iron container \((k=52 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and \(\alpha=1.70 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\) ) with \(4-\mathrm{cm}\)-thick walls is initially at a uniform temperature of \(0^{\circ} \mathrm{C}\) and is filled with ice at \(0^{\circ} \mathrm{C}\). Now the outer surfaces of the container are exposed to hot water at $55^{\circ} \mathrm{C}$ with a very large heat transfer coefficient. Determine how long it will be before the ice inside the container starts melting. Also, taking the heat transfer coefficient on the inner surface of the container to be $250 \mathrm{~W} / \mathrm{m}^{2}\(, \)\mathrm{K}$, determine the rate of heat transfer to the ice through a \(1.2-\mathrm{m}\)-wide and \(2-\mathrm{m}\)-high section of the wall when steady operating conditions are reached. Assume the ice starts melting when its inner surface temperature rises to $0.1^{\circ} \mathrm{C}$.

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.

A 2-cm-diameter plastic rod has a thermocouple inserted to measure temperature at the center of the rod. The plastic rod $\left(\rho=1190 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=1465 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right.$, and \(k=0.19\) \(\mathrm{W} / \mathrm{m} \cdot \mathrm{K}\) ) was initially heated to a uniform temperature of \(70^{\circ} \mathrm{C}\) and allowed to be cooled in ambient air at \(25^{\circ} \mathrm{C}\). After \(1388 \mathrm{~s}\) of cooling, the thermocouple measured the temperature at the center of the rod to be \(30^{\circ} \mathrm{C}\). Determine the convection heat transfer coefficient for this process. Solve this problem using the analytical one-term approximation method.

The 35-cm-thick roof of a large room made of concrete $\left(k=0.79 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \alpha=5.88 \times 10^{-7} \mathrm{~m}^{2} / \mathrm{s}\right)$ is initially at a uniform temperature of \(15^{\circ} \mathrm{C}\). After a heavy snowstorm, the outer surface of the roof remains covered with snow at \(-5^{\circ} \mathrm{C}\). The roof temperature at \(12 \mathrm{~cm}\) distance from the outer surface after $2 \mathrm{~h}$ is (a) \(13^{\circ} \mathrm{C}\) (b) \(11^{\circ} \mathrm{C}\) (c) \(7^{\circ} \mathrm{C}\) (d) \(3^{\circ} \mathrm{C}\) (e) \(-5^{\circ} \mathrm{C}\)

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