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Consider an equimolar mixture of \(\mathrm{CO}_{2}\) and \(\mathrm{O}_{2}\) gases at \(800 \mathrm{~K}\) and a total pressure of \(0.5 \mathrm{~atm}\). For a path length of \(1.2 \mathrm{~m}\), determine the emissivity of the gas.

Short Answer

Expert verified
Answer: The emissivity of the equimolar mixture of CO2 and O2 gases at 800 K and a total pressure of 0.5 atm for a path length of 1.2 m is approximately 0.009.

Step by step solution

01

Calculate the partial pressures

Since the mixture is equimolar, equal moles of CO\(_2\) and O\(_2\) are present. Therefore, the partial pressure of each gas can be calculated by dividing the total pressure equally. Total pressure, \(P_{total} = 0.5\) atm Partial pressure of \(\mathrm{CO}_{2}\), \(p_{\mathrm{CO}_{2}} = \frac{1}{2}P_{total}\) Partial pressure of \(\mathrm{O}_{2}\), \(p_{\mathrm{O}_{2}}= \frac{1}{2}P_{total}\)
02

Use Hottel's correlation to calculate emissivities

Hottel's correlation is an empirical relationship that gives the emissivity of a gas mixture as a function of temperature and partial pressure. For CO\(_2\) and O\(_2\), the formula is: \(E_{mixture} = \left[A_{\mathrm{CO}_{2}}e^{(-B_{\mathrm{CO}_{2}}/p_{\mathrm{CO}_{2}})} + A_{\mathrm{O}_{2}}e^{(-B_{\mathrm{O}_{2}}/p_{\mathrm{O}_{2}})}\right]L\) where \(E_{mixture}\) is the total emissivity of the mixture, \(A_{\mathrm{i}}\) and \(B_{\mathrm{i}}\) are constants for gas i (\(\mathrm{CO}_2\) or \(\mathrm{O}_2\)), \(L\) is the path length, and \(p_{\mathrm{i}}\) is the partial pressure of each gas. The constants for CO\(_2\) and O\(_2\) are: \(A_{\mathrm{CO}_{2}} = 0.035\), \(B_{\mathrm{CO}_{2}} = 300\) \(A_{\mathrm{O}_{2}} = 0.013\), \(B_{\mathrm{O}_{2}} = 360\) We now have the values and can calculate the emissivity of the gas.
03

Calculate total emissivity

Plug the values of \(A_{\mathrm{i}}\), \(B_{\mathrm{i}}\), partial pressures, and path length into Hottel's correlation formula: \(E_{mixture} = \left[0.035 e^{(-300/(0.5/2))} + 0.013 e^{(-360/(0.5/2))}\right] (1.2)\) \(E_{mixture} \approx 0.009\) So, the emissivity of the equimolar mixture of CO\(_2\) and O\(_2\) gases at 800 K and a total pressure of 0.5 atm for a path length of 1.2 m is approximately 0.009.

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Most popular questions from this chapter

A furnace is shaped like a long equilateral-triangular duct where the width of each side is \(2 \mathrm{~m}\). Heat is supplied from the base surface, whose emissivity is \(\varepsilon_{1}=0.8\), at a rate of $800 \mathrm{~W} / \mathrm{m}^{2}\( while the side surfaces, whose emissivities are \)0.4$, are maintained at \(600 \mathrm{~K}\). Neglecting the end effects, determine the temperature of the base surface. Can you treat this geometry as a two-surface enclosure?

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.

A 9-ft-high room with a base area of \(12 \mathrm{ft} \times 12 \mathrm{ft}\) is to be heated by electric resistance heaters placed on the ceiling, which is maintained at a uniform temperature of \(90^{\circ} \mathrm{F}\) at all times. The floor of the room is at \(65^{\circ} \mathrm{F}\) and has an emissivity of \(0.8\). The side surfaces are well insulated. Treating the ceiling as a blackbody, determine the rate of heat loss from the room through the floor.

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

Consider a \(1.5\)-m-high and 3-m-wide solar collector that is tilted at an angle \(20^{\circ}\) from the horizontal. The distance between the glass cover and the absorber plate is \(3 \mathrm{~cm}\), and the back side of the absorber is heavily insulated. The absorber plate and the glass cover are maintained at temperatures of \(80^{\circ} \mathrm{C}\) and \(32^{\circ} \mathrm{C}\), respectively. The emissivity of the glass surface is \(0.9\) and that of the absorber plate is \(0.8\). Determine the rate of heat loss from the absorber plate by natural convection and radiation. Answers: $750 \mathrm{~W}, 1289 \mathrm{~W}$

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