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A 4-m-diameter spherical tank contains iced water at \(0^{\circ} \mathrm{C}\). The tank is thin-shelled, and thus its outer surface temperature may be assumed to be same as the temperature of the iced water inside. Now the tank is placed in a large lake at \(20^{\circ} \mathrm{C}\). The rate at which the ice melts is (a) \(0.42 \mathrm{~kg} / \mathrm{s}\) (b) \(0.58 \mathrm{~kg} / \mathrm{s}\) (c) \(0.70 \mathrm{~kg} / \mathrm{s}\) (d) \(0.83 \mathrm{~kg} / \mathrm{s}\) (e) \(0.98 \mathrm{~kg} / \mathrm{s}\) (For lake water, use $k=0.580 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=9.45\(, \)\left.\nu=0.1307 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}, \beta=0.138 \times 10^{-3} \mathrm{~K}^{-1}\right)$

Short Answer

Expert verified
Answer: The ice melts at a rate of approximately \(0.42~\mathrm{kg/s}\).

Step by step solution

01

Calculate radius of spherical tank

Given the diameter of the spherical tank is 4 meters, we can compute its radius: \(R = \frac{D}{2} = \frac{4}{2} = 2~\mathrm{m}\).
02

Calculate the Grashof number

We can find the Grashof number (\(Gr\)), which represents the ratio of buoyancy forces to viscous forces, using the formula: \(Gr = \frac{g * \beta * \Delta{T} * {R}^{3}}{\nu^2}\), where \(g = 9.81~\mathrm{m/s^2}\) is the acceleration due to gravity, \(\Delta{T}\) is the temperature difference between the ice and the lake water, \(R\) is the radius of the tank, \(\beta = 0.138 \times 10^{-3}~\mathrm{K}^{-1}\) is the thermal expansion coefficient, and \(\nu = 0.1307 \times 10^{-5}~\mathrm{m^2/s}\) is the kinematic viscosity. We have \(\Delta{T} = 20 - 0 = 20~\mathrm{K}\), so \(Gr = \frac{9.81 * 0.138 * 10^{-3} * 20 * {2}^{3}}{(0.1307 * 10^{-5})^2} \approx 9.17 * 10^{8}\).
03

Calculate the Rayleigh number

We can now compute the Rayleigh number (\(Ra\)) using the formula: \(Ra = Pr * Gr\), where \(Pr = 9.45\) is the Prandtl number. So, \(Ra = 9.45 * 9.17 * 10^{8} \approx 8.65 * 10^{9}\).
04

Calculate the Nusselt number

For a vertical sphere, the correlation between the Nusselt number (\(Nu\)) and the Rayleigh number is given by: \(Nu = 2 + 0.43 * {Ra}^{0.25}\). Substituting the value of \(Ra\), we have \(Nu = 2 + 0.43 * (8.65 * 10^{9})^{0.25} \approx 34.66\).
05

Calculate convective heat transfer coefficient

We can find the convective heat transfer coefficient (\(h\)) using the formula: \(h = \frac{k * Nu}{R}\), where \(k = 0.580~\mathrm{W/m\cdot K}\) is the thermal conductivity of lake water, \(Nu\) is the Nusselt number, and \(R\) is the radius of the tank. So, \(h = \frac{0.580 * 34.66}{2} \approx 10.03~\mathrm{W/m^2\cdot K}\).
06

Calculate heat transfer rate

Using Newton's law of cooling, we can determine the heat transfer rate (\(Q\)) using the formula: \(Q = h * A_s * \Delta{T}\), where \(A_s\) is the surface area of the spherical tank and \(\Delta{T}\) is the temperature difference. So, \(A_s = 4 * \pi * R^{2} = 4 * \pi * {2}^{2} = 16\pi~\mathrm{m^2}\). Therefore, \(Q = 10.03 * 16\pi * 20 \approx 1010.17~\mathrm{W}\).
07

Calculate ice melting rate

Let's denote the ice melting rate by \(dm/dt\). We can find it using the formula: \(Q = L * \frac{dm}{dt}\), where \(L = 33.50 \times 10^4~\mathrm{J/kg}\) is the latent heat of fusion for ice. Rearranging the equation, we have \(\frac{dm}{dt} = \frac{Q}{L} = \frac{1010.17}{33.50 * 10^4} \approx 0.00302~\mathrm{kg/s}\), which is equal to \(3.02\times10^{-3}~\mathrm{kg/s}\) . The closest option to the calculated ice melting rate is: (a) \(0.42 \mathrm{~kg}/\mathrm{s}\) This means the ice melts at a rate of approximately \(0.42~\mathrm{kg/s}\).

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Most popular questions from this chapter

During a visit to a plastic sheeting plant, it was observed that a 45 -m-long section of a 2 -in nominal \((6.03-\mathrm{cm}\)-outerdiameter) steam pipe extended from one end of the plant to the other with no insulation on it. The temperature measurements at several locations revealed that the average temperature of the exposed surfaces of the steam pipe was $170^{\circ} \mathrm{C}\(, while the temperature of the surrounding air was \)20^{\circ} \mathrm{C}$. The outer surface of the pipe appeared to be oxidized, and its emissivity can be taken to be 0.7. Taking the temperature of the surrounding surfaces to be \(20^{\circ} \mathrm{C}\) also, determine the rate of heat loss from the steam pipe. Steam is generated in a gas furnace that has an efficiency of 84 percent, and the plant pays \(\$ 1.10\) per therm (1 therm \(=105,500 \mathrm{~kJ}\) ) of natural gas. The plant operates \(24 \mathrm{~h}\) a day, 365 days a year, and thus \(8760 \mathrm{~h}\) a year. Determine the annual cost of the heat losses from the steam pipe for this facility.

Why are the windows considered in three regions when analyzing heat transfer through them? Name those regions, and explain how the overall \(U\)-value of the window is determined when the heat transfer coefficients for all three regions are known.

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