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A 6-cm-diameter, 13-cm-high canned drink \((\rho=977\) $\left.\mathrm{kg} / \mathrm{m}^{3}, k=0.607 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( initially at \)25^{\circ} \mathrm{C}\( is to be cooled to \)5^{\circ} \mathrm{C}$ by dropping it into iced water at \(0^{\circ} \mathrm{C}\). Total surface area and volume of the drink are \(A_{s}=301.6 \mathrm{~cm}^{2}\) and \(V=367.6 \mathrm{~cm}^{3}\). If the heat transfer coefficient is \(120 \mathrm{~W} / \mathrm{m}^{2}, \mathrm{~K}\), determine how long it will take for the drink to cool to $5^{\circ} \mathrm{C}$. Assume the can is agitated in water, and thus the temperature of the drink changes uniformly with time. (a) \(1.5 \mathrm{~min}\) (b) \(8.7 \mathrm{~min}\) (c) \(11.1 \mathrm{~min}\) (d) \(26.6 \mathrm{~min}\) (e) \(6.7 \mathrm{~min}\)

Short Answer

Expert verified
Answer: It takes approximately 8.76 minutes for the canned drink to cool down to 5°C when placed in iced water.

Step by step solution

01

Convert the given values to SI units

To simplify our calculations, convert all values to the SI (International System of Units) system. Diameter: \(6 cm = 0.06 m\) Total surface area: \(A_{s} = 301.6 cm^2 = 0.03016 m^2\) Volume: \(V = 367.6 cm^3 = 3.676\times 10^{-4} m^3\)
02

Determine the mass of the drink

Mass, m, can be determined by the following formula: \(m = \rho V\) Here, \(\rho = 977 kg/m^3\) (density) and \(V = 3.676\times 10^{-4} m^3\) (volume) \(m = 977 \times 3.676\times 10^{-4} = 0.359 kg\)
03

Calculate the time constant

To find out the time constant, τ, we first need to determine the Biot number, \(Bi\), using the following formula: \(Bi = \frac{h L_c}{k}\) where \(L_c = \frac{V}{A_s}\) is the characteristic length, \(h=120 W/m^2K\) is the heat transfer coefficient, and \(k = 0.607 W/mK\) is the thermal conductivity. \(L_c = \frac{3.676\times 10^{-4}}{0.03016} = 0.0122 m\) \(Bi = \frac{120\times 0.0122}{0.607} = 2.414\) Since the Biot number (\(Bi>0.1\)), we cannot directly use the lumped-capacitance method, so we transition to the transient heat conduction approach and calculate the time constant by: \( τ = \frac{ρVc_p}{hA_s}\) where \(ρ = 977 kg/m^3\), \(V= 3.676\times 10^{-4} m^3\), \(c_p = 4180 J/kgK\), \(h = 120 W/m^2K\), and \(A_s = 0.03016 m^2\). \(τ = \frac{977 \times 3.676\times 10^{-4} \times 4180}{120 \times 0.03016} = 452.7 s\)
04

Calculate the time required for cooling

Using the time constant from the previous step, we can calculate the cooling time using the exponential decay formula: \(T(t) = T_\infty + (T_0 - T_\infty) e^{-t/τ}\) where \(T(t)\) is the temperature at time \(t\), \(T_\infty = 0^{\circ}C\) (temperature of the iced water), \(T_0 = 25^{\circ}C\) (initial temperature of the drink), \(t\) is the time that the drink is in the iced water and \(τ = 452.7 s\) is the time constant. We want to find the time \(t\) when \(T(t) = 5^{\circ}C\). Solving the equation for \(t\), we get: \(5 = 0 + (25 - 0) e^{-t/452.7}\) Dividing both sides by 25 gives: \(\frac{1}{5} = e^{-t/452.7}\) Take the natural logarithm of both sides: \(ln(0.2) = -t / 452.7\) Now, solve for \(t\): \(t = -452.7 ln(0.2) = 525.7 s\) Convert seconds to minutes: \(t = \frac{525.7}{60} = 8.76 min\) So, the answer is close to option (b) \(8.7\mathrm{~min}\).

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Most popular questions from this chapter

Citrus fruits are very susceptible to cold weather, and extended exposure to subfreezing temperatures can destroy them. Consider an 8 -cm-diameter orange that is initially at \(15^{\circ} \mathrm{C}\). A cold front moves in one night, and the ambient temperature suddenly drops to \(-6^{\circ} \mathrm{C}\), with a heat transfer coefficient of $15 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Using the properties of water for the orange and assuming the ambient conditions remain constant for \(4 \mathrm{~h}\) before the cold front moves out, determine if any part of the orange will freeze that night. Solve this problem using the analytical one-term approximation method.

Lumped system analysis of transient heat conduction situations is valid when the Biot number is (a) very small (b) approximately one (c) very large (d) any real number (e) cannot say unless the Fourier number is also known

A \(10-\mathrm{cm}\)-thick aluminum plate $\left(\alpha=97.1 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\right)$ is being heated in liquid with temperature of \(500^{\circ} \mathrm{C}\). The aluminum plate has a uniform initial temperature of \(25^{\circ} \mathrm{C}\). If the surface temperature of the aluminum plate is approximately the liquid temperature, determine the temperature at the center plane of the aluminum plate after 15 s of heating. 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.

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 $0.1^{\circ} \mathrm{C}$.

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