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Two parallel disks of diameter \(D=0.6 \mathrm{~m}\) separated by $L=0.4 \mathrm{~m}$ are located directly on top of each other. Both disks are black and are maintained at a temperature of \(450 \mathrm{~K}\). The back sides of the disks are insulated, and the environment that the disks are in can be considered to be blackbodies at \(300 \mathrm{~K}\). Determine the net rate of radiation heat transfer from the disks to the environment. Answer: $781 \mathrm{~W}$

Short Answer

Expert verified
Answer: The net rate of radiation heat transfer from the two parallel black disks to the environment is approximately 781 W.

Step by step solution

01

Determine the emissivity and area of the disks

Since the disks are black, their emissivity (\(\epsilon\)) is equal to 1. We will use the diameter provided to find the area of the disks. The area \(A\) of each disk can be found using the formula for the area of a circle: \(A = \pi (\frac{D}{2})^2\) Plug in the diameter D=0.6 m: \(A = \pi (\frac{0.6}{2})^2 = 0.2827 \mathrm{~m^2}\)
02

Calculate the disks' radiation heat transfer to the environment

In order to calculate the heat transfer, we need to use Stefan-Boltzmann Law, which is: \(q = \epsilon A \sigma (T_1^4 - T_2^4)\) where \(q\) is the net rate of radiation heat transfer, \(\epsilon\) is the emissivity, \(A\) is the area, \(\sigma\) is the Stefan-Boltzmann constant \((5.67\times10^{-8} \mathrm{W/m^2K^4})\), \(T_1\) and \(T_2\) are the temperatures of the disks and the environment, respectively. Using the values provided, we can find the heat transfer per disk: \(q = 1 \times 0.2827 \times 5.67\times10^{-8} \times (450^4 - 300^4)\) \(q \approx 390.53 \mathrm{~W}\)
03

Find the net rate of radiation heat transfer from the disks to the environment

Since both disks are completely similar, their radiation heat transfer will be the same. So the net rate of heat transfer is the sum of the heat transfer rates for the two disks: \(q_\text{total} = 2 \times q = 2 \times 390.53 \) \(q_\text{total} \approx 781.06 \mathrm{~W}\) Since we are looking for the answer in whole numbers, we round the result: Answer: \(q_\text{total} \approx 781\, \mathrm{W}\)

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Most popular questions from this chapter

Two very large parallel plates are maintained at uniform temperatures \(T_{1}=750 \mathrm{~K}\) and \(T_{2}=500 \mathrm{~K}\) and have emissivities \(\varepsilon_{1}=0.85\) and \(\varepsilon_{2}=0.7\), respectively. If a thin aluminum sheet with the same emissivity on both sides is to be placed between the plates in order to reduce the net rate of radiation heat transfer between the plates by 90 percent, the emissivity of the aluminum sheet must be (a) \(0.07\) (b) \(0.10\) (c) \(0.13\) (d) \(0.16\) (e) \(0.19\)

A long cylindrical fuel rod with a diameter of 3 cm is enclosed by a concentric tube with a diameter of \(6 \mathrm{~cm}\). The tube is an ASTM A249 904L stainless steel tube with a maximum use temperature of $260^{\circ} \mathrm{C}$ specified by the ASME Code for Process Piping (ASME B31.3-2014, Table A-1M). The gap between the fuel rod and the tube is a vacuum. The fuel rod has a surface temperature of \(550^{\circ} \mathrm{C}\). The emissivities of the fuel rod and the ASTM A249 904L tube are \(0.97\) and \(0.33\), respectively. The rate of radiation heat transfer per unit length from the fuel rod to the stainless steel tube is \(120 \mathrm{~W} / \mathrm{m}\). A concentric radiation shield with a diameter of \(45 \mathrm{~mm}\) is to be placed in between the fuel rod and the stainless steel tube to keep the temperature of the stainless steel tube from exceeding its maximum use temperature. Determine (a) the emissivity that the radiation shield needs to keep the stainless steel tube from exceeding \(260^{\circ} \mathrm{C}\) and \((b)\) the temperature of the stainless steel tube if there is no radiation shield.

Two coaxial cylinders of diameters \(D_{1}=0.10 \mathrm{~m}\) and $D_{2}=0.50 \mathrm{~m}\( and emissivities \)\varepsilon_{1}=0.7\( and \)\varepsilon_{2}=0.4$ are maintained at uniform temperatures of \(T_{1}=750 \mathrm{~K}\) and \(T_{2}=500 \mathrm{~K}\), respectively. Now a coaxial radiation shield of diameter \(D_{3}=0.20 \mathrm{~m}\) and emissivity \(\varepsilon_{3}=0.2\) is placed between the two cylinders. Determine the net rate of radiation heat transfer between the two cylinders per unit length of the cylinders, and compare the result with that without the shield.

A dryer is shaped like a long semicylindrical duct of diameter $1.5 \mathrm{~m}$. The base of the dryer is occupied by watersoaked materials to be dried, and it is maintained at a temperature of \(370 \mathrm{~K}\) and emissivity of \(0.5\). The dome of the dryer is maintained at \(1000 \mathrm{~K}\) with emissivity of \(0.8\). Determine the drying rate per unit length experienced by the wet materials.

Two coaxial parallel disks of equal diameter \(1 \mathrm{~m}\) are originally placed at a distance of \(1 \mathrm{~m}\) apart. If both disks behave as black surfaces, determine the new distance between the disks such that there is a \(75 \%\) reduction in radiation heat transfer rate from the original distance of \(1 \mathrm{~m}\).

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