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Water is boiling in a 25 -cm-diameter aluminum pan $(k=237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\( at \)95^{\circ} \mathrm{C}$. Heat is transferred steadily to the boiling water in the pan through its \(0.5-\mathrm{cm}\)-thick flat bottom at a rate of \(800 \mathrm{~W}\). If the inner surface temperature of the bottom of the pan is \(108^{\circ} \mathrm{C}\), determine \((a)\) the boiling heat transfer coefficient on the inner surface of the pan and \((b)\) the outer surface temperature of the bottom of the pan.

Short Answer

Expert verified
Answer: The boiling heat transfer coefficient on the inner surface of the pan is 1253.3 W/m²K, and the outer surface temperature of the bottom of the pan is 104.3°C.

Step by step solution

01

Determine the boiling heat transfer coefficient

To determine the boiling heat transfer coefficient (h), we can use the following formula, derived from Fourier's law: \(h = \frac{q''}{(T_{surface} - T_{fluid})}\) where \(q''\) represents the heat flux (W/m²), \(T_{surface}\) is the inner surface temperature (108°C), and \(T_{fluid}\) is the temperature of the boiling water (95°C). First, we need to find the heat flux. Since the total heat transfer rate (Q) is given as 800W, we can find the heat flux: \(q'' = \frac{Q}{A}\) where A is the surface area of the bottom of the pan. We can calculate the surface area as: \(A = \pi (D/2)^2\) where D is the diameter of the pan (25 cm). Now we can calculate the heat flux and coefficient.
02

Calculate heat flux and coefficient

First, let's find the surface area: \(A = \pi (25/2 * 10^{-2})^2 = 0.0491 \: \text{m}^2\) Now we can calculate the heat flux: \(q'' = \frac{800\: \text{W}}{0.0491 \: \text{m}^2} = 16293 \: \frac{\text{W}}{\text{m}^2}\) Now we can calculate the boiling heat transfer coefficient: \(h = \frac{16293\: \frac{\text{W}}{\text{m}^2}}{(108 - 95)^{\circ}\text{C}} = 1253.3 \frac{\text{W}}{\text{m}^2 \cdot \text{K}}\)
03

Determine the outer surface temperature

For this part, we will use the heat conduction equation: \(q'' = k \frac{(T_{in} - T_{out})}{L}\) where k is the thermal conductivity of aluminum (237 W/m⋅K), \(T_{in}\) is the inner surface temperature (108°C), \(T_{out}\) is the outer surface temperature (which we want to determine), and L is the thickness of the bottom of the pan (0.5 cm = 0.005 m). Solving for \(T_{out}\), we get: \(T_{out} = T_{in} - \frac{q'' \cdot L}{k}\) Now we can calculate the outer surface temperature.
04

Calculate outer surface temperature

Now we can plug in the numbers to find the outer surface temperature: \(T_{out} = 108^{\circ}\text{C} - \frac{16293 \: \frac{\text{W}}{\text{m}^2} \cdot 0.005 \: \text{m}}{237 \: \frac{\text{W}}{\text{m} \cdot \text{K}}} = 104.3^{\circ} \mathrm{C}\)
05

Summary of results:

(a) The boiling heat transfer coefficient on the inner surface of the pan is \(1253.3 \frac{\text{W}}{\text{m}^2 \cdot \text{K}}\). (b) The outer surface temperature of the bottom of the pan is \(104.3^{\circ} \mathrm{C}\).

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Most popular questions from this chapter

A turbine blade made of a metal alloy $(k=17 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\( has a length of \)5.3 \mathrm{~cm}\(, a perimeter of \)11 \mathrm{~cm}\(, and a crosssectional area of \)5.13 \mathrm{~cm}^{2}$. The turbine blade is exposed to hot gas from the combustion chamber at \(973^{\circ} \mathrm{C}\) with a convection heat transfer coefficient of $538 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. The base of the turbine blade maintains a constant temperature of \(450^{\circ} \mathrm{C}\), and the tip is adiabatic. Determine the heat transfer rate to the turbine blade and the temperature at the tip.

Circular fins of uniform cross section, with diameter of \(10 \mathrm{~mm}\) and length of \(50 \mathrm{~mm}\), are attached to a wall with surface temperature of \(350^{\circ} \mathrm{C}\). The fins are made of material with thermal conductivity of \(240 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), they are exposed to an ambient air condition of \(25^{\circ} \mathrm{C}\), and the convection heat transfer coefficient is $250 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Determine the heat transfer rate and plot the temperature variation of a single fin for the following boundary conditions: (a) Infinitely long fin (b) Adiabatic fin tip (c) Fin with tip temperature of \(250^{\circ} \mathrm{C}\) (d) Convection from the fin tip

Hot water at an average temperature of \(53^{\circ} \mathrm{C}\) and an average velocity of \(0.4 \mathrm{~m} / \mathrm{s}\) is flowing through a \(5-\mathrm{m}\) section of a thin-walled hot-water pipe that has an outer diameter of $2.5 \mathrm{~cm}\(. The pipe passes through the center of a \)14-\mathrm{cm}$-thick wall filled with fiberglass insulation $(k=0.035 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\(. If the surfaces of the wall are at \)18^{\circ} \mathrm{C}\(, determine \)(a)$ the rate of heat transfer from the pipe to the air in the rooms and \((b)\) the temperature drop of the hot water as it flows through this 5 -m-long section of the wall.

Two finned surfaces with long fins are identical, except that the convection heat transfer coefficient for the first finned surface is twice that of the second one. Which of the following conditions is accurate for the efficiency and effectiveness of the first finned surface relative to the second one? (a) Higher efficiency and higher effectiveness (b) Higher efficiency but lower effectiveness (c) Lower efficiency but higher effectiveness (d) Lower efficiency and lower effectiveness (e) Equal efficiency and equal effectiveness

A 25-cm-diameter, 2.4-m-long vertical cylinder containing ice at $0^{\circ} \mathrm{C}$ is buried right under the ground. The cylinder is thin-shelled and is made of a high-thermal-conductivity material. The surface temperature and the thermal conductivity of the ground are \(18^{\circ} \mathrm{C}\) and $0.85 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$, respectively. The rate of heat transfer to the cylinder is (a) \(37.2 \mathrm{~W}\) (b) \(63.2 \mathrm{~W}\) (c) \(158 \mathrm{~W}\) (d) \(480 \mathrm{~W}\) (e) \(1210 \mathrm{~W}\)

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