4-115 A semi-infinite aluminum cylinder \((k=237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), \(\left.\alpha=9.71 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\right)\) of diameter \(D=15 \mathrm{~cm}\) is initially at a uniform temperature of \(T_{i}=115^{\circ} \mathrm{C}\). The cylinder is now placed in water at \(10^{\circ} \mathrm{C}\), where heat transfer takes place by convection with a heat transfer coefficient of \(h=140 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Determine the temperature at the center of the cylinder \(5 \mathrm{~cm}\) from the end surface 8 min after the start of cooling. 4-116 A 20-cm-long cylindrical aluminum block \((\rho=\) \(2702 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=0.896 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}, k=236 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and \(\alpha=\) \(\left.9.75 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\right), 15 \mathrm{~cm}\) in diameter, is initially at a uniform temperature of \(20^{\circ} \mathrm{C}\). The block is to be heated in a furnace at \(1200^{\circ} \mathrm{C}\) until its center temperature rises to \(300^{\circ} \mathrm{C}\). If the heat transfer coefficient on all surfaces of the block is \(80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine how long the block should be kept in the furnace. Also, determine the amount of heat transfer from the aluminum block if it is allowed to cool in the room until its temperature drops to \(20^{\circ} \mathrm{C}\) throughout.

Short Answer

Expert verified
Answer: The block should be kept in the furnace for 808.3 seconds for the center temperature to reach 300°C. The total amount of heat transfer from the block if it is allowed to cool down to 20°C would be -8.98 x 10^6 J.

Step by step solution

01

List the given parameters

- Initial temperature of the block, \(T_i = 20^{\circ}\mathrm{C}\) - Length of the block, \(L = 20 \,\mathrm{cm} = 0.2 \,\mathrm{m}\) - Diameter of the block, \(D = 15 \,\mathrm{cm} = 0.15 \,\mathrm{m}\) - Density of aluminum, \(\rho = 2702 \,\mathrm{kg/m^3}\) - Specific heat capacity, \(c_p = 0.896 \,\mathrm{kJ/kg\cdot K} = 896 \,\mathrm{J/kg\cdot K}\) - Thermal conductivity, \(k = 236\,\mathrm{W/m\cdot K}\) - Thermal diffusivity, \(\alpha = 9.75 \times 10^{-5}\,\mathrm{m^2/s}\) - Furnace temperature, \(T_f = 1200^{\circ}\mathrm{C}\) - Desired center temperature, \(T_c = 300^{\circ}\mathrm{C}\) - Heat transfer coefficient, \(h = 80\,\mathrm{W/m^2\cdot K}\)
02

Find the Bi and Fourier Numbers

We need to find the Biot Number \((\mathrm{Bi})\) and Fourier number \((\mathrm{Fo})\) in order to use the heat transfer equation effectively. The Biot Number is given by: $$ \mathrm{Bi}=\frac{h \cdot L_c}{k}=\frac{h(D/2)}{k} $$ The Fourier number is given by: $$ \mathrm{Fo}=\frac{\alpha \cdot t}{L_c^2}=\frac{\alpha \cdot t}{(D/2)^2} $$ We need to find the value of time \(t\) that satisfies both the Biot and Fourier numbers such that the desired center temperature \(T_c = 300^{\circ}\mathrm{C}\) is achieved.
03

Apply the lumped heat capacity method

Since we don't know the required time \(t\), we can use the lumped heat capacity method, which states that: $$ \frac{T(t)-T_i}{T_f-T_i} = e^{-\mathrm{Bi\cdot Fo}} $$ We can rearrange the formula to solve for time \(t\): $$ t = \frac{(D/2)^2}{\alpha}ln\left(\frac{T_f-T_i}{T_c-T_i}\right) $$
04

Calculate the time

Substitute the given values into the equation: $$ t = \frac{(0.15/2)^2}{9.75 \times 10^{-5}}ln\left(\frac{1200-20}{300-20}\right) $$ Calculate the result: $$ t = 808.3 \,\mathrm{s} $$
05

Calculate the total heat transfer

To find the total heat transfer from the block, we use the formula: $$ Q = mc_p\Delta T = \rho Vc_p(T_i - T_c) $$ Where: $$ V = \pi(D/2)^2L $$ Calculate the volume and heat transfer: $$ V = \pi(0.15/2)^2(0.2) = 0.00353 \,\mathrm{m^3} $$ $$ Q = 2702\cdot 0.00353\cdot 896\cdot(20-300) = -8.98\times10^{6} \,\mathrm{J} $$ #Results# The block should be kept in the furnace for \(808.3\,\mathrm{s}\) in order for the center temperature to rise to \(300^{\circ}\mathrm{C}\). The total amount of heat transfer from the block if it is allowed to cool down to \(20^{\circ}\mathrm{C}\) would be \(-8.98\times 10^{6}\,\mathrm{J}\).

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Most popular questions from this chapter

Consider the freezing of packaged meat in boxes with refrigerated air. How do \((a)\) the temperature of air, (b) the velocity of air, \((c)\) the capacity of the refrigeration system, and \((d)\) the size of the meat boxes affect the freezing time?

For heat transfer purposes, an egg can be considered to be a \(5.5-\mathrm{cm}\)-diameter sphere having the properties of water. An egg that is initially at \(8^{\circ} \mathrm{C}\) is dropped into the boiling water at \(100^{\circ} \mathrm{C}\). The heat transfer coefficient at the surface of the egg is estimated to be \(800 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). If the egg is considered cooked when its center temperature reaches \(60^{\circ} \mathrm{C}\), determine how long the egg should be kept in the boiling water. Solve this problem using analytical one-term approximation method (not the Heisler charts).

A body at an initial temperature of \(T_{i}\) is brought into a medium at a constant temperature of \(T_{\infty}\). How can you determine the maximum possible amount of heat transfer between the body and the surrounding medium?

A long cylindrical wood \(\log (k=0.17 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and \(\left.\alpha=1.28 \times 10^{-7} \mathrm{~m}^{2} / \mathrm{s}\right)\) is \(10 \mathrm{~cm}\) in diameter and is initially at a uniform temperature of \(15^{\circ} \mathrm{C}\). It is exposed to hot gases at \(550^{\circ} \mathrm{C}\) in a fireplace with a heat transfer coefficient of \(13.6 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) on the surface. If the ignition temperature of the wood is \(420^{\circ} \mathrm{C}\), determine how long it will be before the log ignites. Solve this problem using analytical one-term approximation method (not the Heisler charts).

Carbon steel balls ( \(\rho=7830 \mathrm{~kg} / \mathrm{m}^{3}, k=64 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), \(\left.c_{p}=434 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) initially at \(150^{\circ} \mathrm{C}\) are quenched in an oil bath at \(20^{\circ} \mathrm{C}\) for a period of 3 minutes. 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) \(27.4^{\circ} \mathrm{C}\) (b) \(143^{\circ} \mathrm{C}\) (c) \(12.7^{\circ} \mathrm{C}\) (d) \(48.2^{\circ} \mathrm{C}\) (e) \(76.9^{\circ} \mathrm{C}\)

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