Chapter 13: Problem 124
What is operative temperature? How is it related to the mean ambient and radiant temperatures? How does it differ from effective temperature?
Chapter 13: Problem 124
What is operative temperature? How is it related to the mean ambient and radiant temperatures? How does it differ from effective temperature?
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Get started for freeTwo very large parallel plates are maintained at uniform temperatures of \(T_{1}=600 \mathrm{~K}\) and \(T_{2}=400 \mathrm{~K}\) and have emissivities \(\varepsilon_{1}=0.5\) and \(\varepsilon_{2}=0.9\), respectively. Determine the net rate of radiation heat transfer between the two surfaces per unit area of the plates.
A furnace is shaped like a long semicylindrical duct of diameter $D=15 \mathrm{ft}\(. The base and the dome of the furnace have emissivities of \)0.5$ and \(0.9\) and are maintained at uniform temperatures of 550 and $1800 \mathrm{R}$, respectively. Determine the net rate of radiation heat transfer from the dome to the base surface per unit length during steady operation.
A 2-m-internal-diameter double-walled spherical tank is used to store iced water at \(0^{\circ} \mathrm{C}\). Each wall is \(0.5 \mathrm{~cm}\) thick, and the \(1.5-\mathrm{cm}\)-thick airspace between the two walls of the tank is evacuated in order to minimize heat transfer. The surfaces surrounding the evacuated space are polished so that each surface has an emissivity of \(0.15\). The temperature of the outer wall of the tank is measured to be $20^{\circ} \mathrm{C}\(. Assuming the inner wall of the steel tank to be at \)0^{\circ} \mathrm{C}\(, determine \)(a)$ the rate of heat transfer to the iced water in the tank and \((b)\) the amount of ice at \(0^{\circ} \mathrm{C}\) that melts during a 24 -h period.
The base surface of a cubical furnace with a side length of \(3 \mathrm{~m}\) has an emissivity of \(0.80\) and is maintained at \(500 \mathrm{~K}\). If the top and side surfaces also have an emissivity of \(0.80\) and are maintained at $900 \mathrm{~K}$, the net rate of radiation heat transfer from the top and side surfaces to the bottom surface is (a) \(194 \mathrm{~kW}\) (b) \(233 \mathrm{~kW}\) (c) \(288 \mathrm{~kW}\) (d) \(312 \mathrm{~kW}\) (e) \(242 \mathrm{~kW}\)
Cryogenic fluid flows inside a 10-mm-diameter metal tube. The metal tube is enclosed by a concentric polypropylene tube with a diameter of \(15 \mathrm{~mm}\). The minimum temperature limit for polypropylene tube is \(-18^{\circ} \mathrm{C}\), specified by the ASME Code for Process Piping (ASME B31.3-2014, Table B-1). The gap between the concentric tubes is a vacuum. The inner metal tube and the outer polypropylene tube have emissivity values of \(0.5\) and \(0.97\), respectively. The concentric tubes are placed in a vacuum environment, where the temperature of the surroundings is \(0^{\circ} \mathrm{C}\). Determine the lowest temperature that the inner metal tube can go without cooling the polypropylene tube below its minimum temperature limit of $-18^{\circ} \mathrm{C}$. Assume both tubes have thin walls.
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