Consider a cubic block whose sides are \(5 \mathrm{~cm}\) long and a cylindrical block whose height and diameter are also \(5 \mathrm{~cm}\). Both blocks are initially at \(20^{\circ} \mathrm{C}\) and are made of granite \((k=\) \(2.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and \(\left.\alpha=1.15 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\right)\). Now both blocks are exposed to hot gases at \(500^{\circ} \mathrm{C}\) in a furnace on all of their surfaces with a heat transfer coefficient of \(40 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Determine the center temperature of each geometry after 10,20 , and \(60 \mathrm{~min}\).

Short Answer

Expert verified
Based on the given problem and solution, a short answer question can be created as follows: Question: Two blocks - a cubic block and a cylindrical block made of granite are exposed to hot gases at \(500^{\circ} \mathrm{C}\). The length of the cubic block and the height and diameter of the cylindrical block are \(5 \mathrm{~cm}\). Both blocks have an initial temperature of \(20^{\circ} \mathrm{C}\). Using the lumped capacitance method, determine the center temperature of each block after 10, 20, and 60 minutes. (Given: \(k=2.5\ \mathrm{W} / \mathrm{m} \cdot \mathrm{K}\), \(\alpha=1.15 \times 10^{-6}\ \mathrm{m}^{2} / \mathrm{s}\), heat transfer coefficient \(40\ \mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}\), granite density \(\rho\approx 2700\ \mathrm{kg}/\mathrm{m}^3\), and specific heat \(c_p\approx 790\ \mathrm{J}/\mathrm{kg \cdot K}\).) Answer: *Before providing the final answer, make sure to follow the steps provided in the solution, calculate the Biot number for each block, and check if the lumped capacitance method can be used.* For the cubic block: - \(T_{cube}(10\ \mathrm{min}) = ...^{\circ} \mathrm{C}\) - \(T_{cube}(20\ \mathrm{min}) = ...^{\circ} \mathrm{C}\) - \(T_{cube}(60\ \mathrm{min}) = ...^{\circ} \mathrm{C}\) For the cylindrical block: - \(T_{cylinder}(10\ \mathrm{min}) = ...^{\circ} \mathrm{C}\) - \(T_{cylinder}(20\ \mathrm{min}) = ...^{\circ} \mathrm{C}\) - \(T_{cylinder}(60\ \mathrm{min}) = ...^{\circ} \mathrm{C}\)

Step by step solution

01

Characteristic Length (Cubic Block)

The characteristic length for a cube is given by the formula \(L_c = \frac{V}{A} = \frac{l^3}{6l^2}=\frac{l}{6}\), where \(l\) is the length of the cube. Since the length is given as \(5\ \mathrm{cm}\), we find the characteristic length: \(L_c = \frac{5}{6}\ \mathrm{cm}\).
02

Characteristic Length (Cylindrical Block)

The characteristic length for a cylinder is given by the formula \(L_c = \frac{V}{A} = \frac{\pi r^2 h}{2\pi r h + 2\pi r^2}\), where \(r\) is the radius and \(h\) is the height of the cylinder. Using diameter \(5\ \mathrm{cm}\), we find the characteristic length: \(L_c = \frac{\pi (2.5)^2 (5)}{2\pi (2.5) (5) + 2\pi (2.5)^2}\).
03

Biot number (Cubic Block)

Now we can calculate the Biot number for the cubic block: \(Bi_{cube} = \frac{40\ \mathrm{W} / \mathrm{m}^2 \cdot \mathrm{K} \times (\frac{5}{6} \times 10^{-2}\ \mathrm{m})}{2.5\ \mathrm{W} / \mathrm{m} \cdot \mathrm{K}}\).
04

Biot number (Cylindrical Block)

Similarly, we can calculate the Biot number for the cylindrical block: \(Bi_{cylinder} = \frac{40\ \mathrm{W} / \mathrm{m}^2 \cdot \mathrm{K} \times L_c}{2.5\ \mathrm{W} / \mathrm{m} \cdot \mathrm{K}}\). Make sure to use the previously calculated value for \(L_c\). Step 2: Use the lumped capacitance method for temperature calculation The lumped capacitance method can be used if \(Bi \le 0.1\). Let's check the calculated Biot numbers for both blocks. If \(Bi\) values are less than or equal to 0.1, we can proceed with the lumped capacitance method. The formula for the lumped capacitance method is: \(T(t) - T_\infty = (T_0 - T_\infty)e^{-\frac{hA}{\rho c_p V}t}\), where \(T(t)\) is the temperature at time \(t\), \(T_\infty\) is the surrounding temperature, \(T_0\) is the initial temperature, \(\rho\) is the density, \(c_p\) is the specific heat, and \(V\) is the volume of the block. We are given that \(T_\infty = 500^{\circ} \mathrm{C}\) and \(T_0 = 20^{\circ} \mathrm{C}\). For granite, we find the density \((\rho\approx 2700\ \mathrm{kg}/\mathrm{m}^3)\) and specific heat \((c_p\approx 790\ \mathrm{J}/\mathrm{kg \cdot K})\) from the reference sources. Now, we can calculate the temperature at the center of each block after 10, 20, and 60 minutes. Make sure to convert the time to seconds.
05

Temperature Calculation (Cubic Block)

Using the lumped capacitance formula and the properties of granite, calculate \(T_{cube}(10\ \mathrm{min})\), \(T_{cube}(20\ \mathrm{min})\), and \(T_{cube}(60\ \mathrm{min})\). Make sure to use the volume and area for a cubic block in calculations.
06

Temperature Calculation (Cylindrical Block)

Similarly, using the lumped capacitance formula and the properties of granite, calculate \(T_{cylinder}(10\ \mathrm{min})\), \(T_{cylinder}(20\ \mathrm{min})\), and \(T_{cylinder}(60\ \mathrm{min})\). Make sure to use the volume and area for a cylindrical block in calculations.

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Most popular questions from this chapter

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 analytical one-term approximation method (not the Heisler charts).

Consider a 7.6-cm-diameter cylindrical lamb meat chunk \(\left(\rho=1030 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=3.49 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}, k=0.456 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right.\), \(\left.\alpha=1.3 \times 10^{-7} \mathrm{~m}^{2} / \mathrm{s}\right)\). Such a meat chunk intially at \(2^{\circ} \mathrm{C}\) is dropped into boiling water at \(95^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(1200 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The time it takes for the center temperature of the meat chunk to rise to \(75{ }^{\circ} \mathrm{C}\) is (a) \(136 \mathrm{~min}\) (b) \(21.2 \mathrm{~min}\) (c) \(13.6 \mathrm{~min}\) (d) \(11.0 \mathrm{~min}\) (e) \(8.5 \mathrm{~min}\)

It is claimed that beef can be stored for up to two years at \(-23^{\circ} \mathrm{C}\) but no more than one year at \(-12^{\circ} \mathrm{C}\). Is this claim reasonable? Explain.

Chickens with an average mass of \(2.2 \mathrm{~kg}\) and average specific heat of \(3.54 \mathrm{~kJ} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}\) are to be cooled by chilled water that enters a continuous-flow-type immersion chiller at \(0.5^{\circ} \mathrm{C}\). Chickens are dropped into the chiller at a uniform temperature of \(15^{\circ} \mathrm{C}\) at a rate of 500 chickens per hour and are cooled to an average temperature of \(3^{\circ} \mathrm{C}\) before they are taken out. The chiller gains heat from the surroundings at a rate of \(210 \mathrm{~kJ} / \mathrm{min}\). Determine \((a)\) the rate of heat removal from the chicken, in \(\mathrm{kW}\), and \((b)\) the mass flow rate of water, in \(\mathrm{kg} / \mathrm{s}\), if the temperature rise of water is not to exceed \(2^{\circ} \mathrm{C}\).

The Biot number during a heat transfer process between a sphere and its surroundings is determined to be \(0.02\). Would you use lumped system analysis or the transient temperature charts when determining the midpoint temperature of the sphere? Why?

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