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A cylindrical container whose height and diameter are \(8 \mathrm{~m}\) is filled with a mixture of \(\mathrm{CO}_{2}\) and \(\mathrm{N}_{2}\) gases at $600 \mathrm{~K}\( and 1 atm. The partial pressure of \)\mathrm{CO}_{2}$ in the mixture is \(0.15 \mathrm{~atm}\). If the walls are black at a temperature of \(450 \mathrm{~K}\), determine the rate of radiation heat transfer between the gas and the container walls.

Short Answer

Expert verified
The rate of radiation heat transfer between the gas and the container walls is approximately 33117.6 W.

Step by step solution

01

Find the partial pressure of nitrogen gas in the mixture

Since the total pressure of the mixture is 1 atm, and the partial pressure of \(\mathrm{CO}_{2}\) is given as \(0.15\mathrm{~atm}\), we can subtract the partial pressure of \(\mathrm{CO}_{2}\) from the total pressure to get the partial pressure of nitrogen gas in the mixture: Partial Pressure of \(\mathrm{N}_{2} = \text{Total Pressure} - \text{Partial Pressure of }\mathrm{CO}_{2}\) \(P_{\mathrm{N}_{2}} = 1\mathrm{~atm} - 0.15\mathrm{~atm}\) \(P_{\mathrm{N}_{2}} = 0.85\mathrm{~atm}\)
02

Calculate the Stefan-Boltzmann constant

The Stefan-Boltzmann constant is denoted by \(\sigma\) and has a value of \(5.67 \times 10^{-8} \frac{\mathrm{W}}{\mathrm{m}^2\mathrm{K}^4}\).
03

Calculate the surface area of the container

To calculate the surface area of the cylindrical container, we need to find the area of the lateral surface and the top and bottom surfaces. The lateral surface area is given by the formula: \(A_{\text{lateral}} = 2 \pi r h\) Where \(r\) is the radius (\(r = \frac{\text{diameter}}{2} = 4\mathrm{~m}\)), and \(h\) is the height of the container (\(h = 8\mathrm{~m}\)). The top and bottom surface areas are given by the formula: \(A_{\text{top/bottom}} = \pi r^2\) Adding them together, we get the total surface area: \(A_{\text{total}} = A_{\text{lateral}} + 2 \times A_{\text{top/bottom}}\)
04

Calculate the rate of radiation heat transfer

Now, we can apply the radiative heat transfer equation: \(Q = \sigma A_{\text{total}} (T_{\text{gas}}^4 - T_{\text{wall}}^4)\) Substitute the values (making sure to use Kelvin for temperatures): \(Q = (5.67 \times 10^{-8} \frac{\mathrm{W}}{\mathrm{m}^2\mathrm{K}^4})(2\pi(4\mathrm{~m})(8\mathrm{~m}) + 2 \times \pi (4\mathrm{~m})^2)((600\mathrm{~K})^4 - (450\mathrm{~K})^4)\) Calculate the result: \(Q \approx 33117.6\mathrm{~W}\) So, the rate of radiation heat transfer between the gas and the container walls is approximately \(33117.6\mathrm{~W}\).

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Most popular questions from this chapter

Two concentric spheres of diameters \(D_{1}=0.3 \mathrm{~m}\) and $D_{2}=0.6 \mathrm{~m}\( are maintained at uniform temperatures \)T_{1}=800 \mathrm{~K}$ and \(T_{2}=500 \mathrm{~K}\) and have emissivities \(\varepsilon_{1}=0.5\) and \(\varepsilon_{2}=0.7\), respectively. Determine the net rate of radiation heat transfer between the two spheres. Also, determine the convection heat transfer coefficient at the outer surface if both the surrounding medium and the surrounding surfaces are at \(30^{\circ} \mathrm{C}\). Assume the emissivity of the outer surface is \(0.35\).

Define the spectral transmissivity of a medium of thickness \(L\) in terms of \((a)\) spectral intensities and \((b)\) the spectral absorption coefficient.

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) \(242 \mathrm{~kW}\)

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 \(1 \mathrm{~m}\).

Consider a gray and opaque surface at \(0^{\circ} \mathrm{C}\) in an environment at \(25^{\circ} \mathrm{C}\). The surface has an emissivity of \(0.8\). If the radiation incident on the surface is \(240 \mathrm{~W} / \mathrm{m}^{2}\), the radiosity of the surface is (a) \(38 \mathrm{~W} / \mathrm{m}^{2}\) (b) \(132 \mathrm{~W} / \mathrm{m}^{2}\) (c) \(240 \mathrm{~W} / \mathrm{m}^{2}\) (d) \(300 \mathrm{~W} / \mathrm{m}^{2}\) (e) \(315 \mathrm{~W} / \mathrm{m}^{2}\)

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