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A long nickel alloy (ASTM B335) cylindrical rod is used as a component in high-temperature process equipment. The rod has a diameter of $5 \mathrm{~cm}\(; its thermal conductivity, specific heat, and density are \)11 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, 380 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\(, and \)9.3 \mathrm{~g} / \mathrm{cm}^{3}$, respectively. Occasionally, the rod is submerged in hot fluid for several minutes, where the fluid temperature is \(500^{\circ} \mathrm{C}\) with a convection heat transfer coefficient of \(440 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The ASME Code for Process Piping limits the maximum use temperature for ASTM B335 rod to \(427^{\circ} \mathrm{C}\) (ASME B31.32014 , Table A-1M). If the initial temperature of the rod is \(20^{\circ} \mathrm{C}\), how long can the rod be submerged in the hot fluid before reaching its maximum use temperature?

Short Answer

Expert verified
The nickel alloy rod can be submerged in the hot fluid for approximately 7024.58 seconds or around 117 minutes before reaching its maximum use temperature.

Step by step solution

01

Calculate the surface area of the rod

We are given the diameter of the rod, which is \(5 \mathrm{~cm}\). The surface area of a cylindrical rod can be calculated using the formula \(A = \pi d L\), where \(d\) is the diameter and \(L\) is the length of the rod. As the rod is long, we can assume that the entire length is in contact with the fluid. Therefore, we can calculate the surface area per unit length, which can be represented as \(A = \pi d\). Now, we can plug in the diameter value to get the surface area per unit length: \(A = \pi(0.05 \mathrm{~m})\) \(A \approx 0.157 \mathrm{~m^2/m}\)
02

Converting the density from g/cm³ to kg/m³

We need to convert the density from grams per cubic centimeter to kilograms per cubic meter: \(\rho = 9.3 \mathrm{~g/cm^3} * \frac{1000 \mathrm{~kg}}{10^6 \mathrm{~g}} * \left(\frac{100 \mathrm{~cm}}{1 \mathrm{~m}}\right)^{3}\) \(\rho = 9300 \mathrm{~kg/m^3}\)
03

Calculate the time by applying the lumped capacitance formula

Now, we have all the necessary parameters to apply the lumped capacitance formula to calculate the time required for the rod to reach its maximum use temperature. Plug in the values given in the problem: \(t = \frac{hA(T_\infty - T_i)}{-kA(T_\infty - T_s)} \tau\) Using the property values for the ASTM B335 rod: \(t = \frac{440 \mathrm{~W/m^2K} * (500^{\circ}\mathrm{C} - 20^{\circ}\mathrm{C})}{-11 \mathrm{~W/mK} * (500^{\circ}\mathrm{C} - 427^{\circ}\mathrm{C})} \tau\) Now, solve for the dimensionless heat transfer time \(\tau\): \(\tau = \frac{440 * 0.157 * (500 - 20)}{-11 * 0.157 * (500 - 427)}\) \(\tau \approx 44.93\)
04

Calculate the time required to reach the maximum use temperature

The final step is to calculate the time \(t\) using the dimensionless heat transfer time \(\tau\) that we just calculated: \(t = \frac{\rho V C_p}{hA} \tau\) We have \(\rho\), \(A\), and \(C_p\) given, so we can assume a unit volume \(V = 1 \mathrm{~m^3}\): \(t = \frac{9300 * 1 * 380}{440 * 0.157} \tau\) \(t \approx 44.93 \times 156.14 \mathrm{~s}\) Finally, calculate the time \(t\) in seconds: \(t \approx 7024.58 \mathrm{~s}\) Thus, the rod can be submerged in the hot fluid for approximately \(7024.58\) seconds or around \(117\) minutes before reaching its maximum use temperature.

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Most popular questions from this chapter

During a fire, the trunks of some dry oak trees $\left(k=0.17 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right.\( and \)\left.\alpha=1.28 \times 10^{-7} \mathrm{~m}^{2} / \mathrm{s}\right)$ that are initially at a uniform temperature of \(30^{\circ} \mathrm{C}\) are exposed to hot gases at \(600^{\circ} \mathrm{C}\) for a period of \(4 \mathrm{~h}\), with a heat transfer coefficient of \(65 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) on the surface. The ignition temperature of the trees is \(410^{\circ} \mathrm{C}\). Treating the trunks of the trees as long cylindrical rods of diameter $20 \mathrm{~cm}$, determine if these dry trees will ignite as the fire sweeps through them. Solve this problem using the analytical one-term approximation method.

Long cylindrical AISI stainless steel rods $\left(k=7.74 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{\circ} \mathrm{F}\right.$ and \(\left.\alpha=0.135 \mathrm{ft}^{2} / \mathrm{h}\right)\) of 4 -in diameter are heat treated by drawing them at a velocity of \(7 \mathrm{ft} / \mathrm{min}\) through a 21 -ft-long oven maintained at \(1700^{\circ} \mathrm{F}\). The heat transfer coefficient in the oven is $20 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}$. If the rods enter the oven at \(70^{\circ} \mathrm{F}\), determine their centerline temperature when they leave. Solve this problem using the analytical one-term approximation method.

In Betty Crocker's Cookbook, it is stated that it takes $2 \mathrm{~h} \mathrm{} 45 \mathrm{~min}\( to roast a \)3.2-\mathrm{kg}$ rib initially at \(4.5^{\circ} \mathrm{C}\) to "rare" in an oven maintained at $163^{\circ} \mathrm{C}$. It is recommended that a meat thermometer be used to monitor the cooking, and the rib is considered rare when the thermometer inserted into the center of the thickest part of the meat registers \(60^{\circ} \mathrm{C}\). The rib can be treated as a homogeneous spherical object with the properties $\rho=1200 \mathrm{~kg} / \mathrm{m}^{3}, c_{p}=4.1 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}, k=0.45 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$, and \(\alpha=0.91 \times 10^{-7} \mathrm{~m}^{2} / \mathrm{s}\). Determine \((a)\) the heat transfer coefficient at the surface of the rib; \((b)\) the temperature of the outer surface of the rib when it is done; and \((c)\) the amount of heat transferred to the rib. \((d)\) Using the values obtained, predict how long it will take to roast this rib to "medium" level, which occurs when the innermost temperature of the rib reaches \(71^{\circ} \mathrm{C}\). Compare your result to the listed value of \(3 \mathrm{~h} \mathrm{} 20 \mathrm{~min} .\) If the roast rib is to be set on the counter for about \(15 \mathrm{~min}\) before it is sliced, it is recommended that the rib be taken out of the oven when the thermometer registers about \(4^{\circ} \mathrm{C}\) below the indicated value because the rib will continue cooking even after it is taken out of the oven. Do you agree with this recommendation? Solve this problem using the analytical one-term approximation method. Answers: (a) $156.9 \mathrm{~W} / \mathrm{m}^{2}-\mathrm{K}\(, (b) \)159.5^{\circ} \mathrm{C}$, (c) \(1629 \mathrm{~kJ}\), (d) \(3.0 \mathrm{~h}\)

A man is found dead in a room at \(12^{\circ} \mathrm{C}\). The surface temperature on his waist is measured to be \(23^{\circ} \mathrm{C}\), and the heat transfer coefficient is estimated to be $9 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. Modeling the body as a \)28-\mathrm{cm}$ diameter, \(1.80\)-m-long cylinder, estimate how long it has been since he died. Take the properties of the body to be $k=0.62 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\( and \)\alpha=0.15 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}$, and assume the initial temperature of the body to be \(36^{\circ} \mathrm{C}\). Solve this problem using the analytical one-term approximation method.

The walls of a furnace are made of \(1.5\)-ft-thick concrete $\left(k=0.64 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}\right.\( and \)\left.\alpha=0.023 \mathrm{ft}^{2} / \mathrm{h}\right)$. Initially, the furnace and the surrounding air are in thermal equilibrium at \(70^{\circ} \mathrm{F}\). The furnace is then fired, and the inner surfaces of the furnace are subjected to hot gases at $1800^{\circ} \mathrm{F}$ with a very large heat transfer coefficient. Determine how long it will take for the temperature of the outer surface of the furnace walls to rise to \(70.1^{\circ} \mathrm{F}\). Answer: \(3.0 \mathrm{~h}\)

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