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How can you determine the view factor \(F_{12}\) when the view factor \(F_{21}\) and the surface areas are available?

Short Answer

Expert verified
Answer: By substituting the given values into the equation, we can determine \(F_{12}\) as follows: $$F_{12} = \frac{F_{21} A_2}{A_1} = \frac{0.6 * 6 m^2}{4 m^2} = \frac{3.6 m^2}{4 m^2} = 0.9$$ Hence, the view factor from surface 1 to surface 2, \(F_{12}\), is 0.9.

Step by step solution

01

Apply the Reciprocity Theorem

According to the reciprocity theorem, we have: $$F_{12} A_1 = F_{21} A_2$$
02

Rearrange the equation to find \(F_{12}\)

We are supposed to find the view factor \(F_{12}\). So, we can rearrange the equation as follows: $$F_{12} = \frac{F_{21} A_2}{A_1}$$
03

Substitute the given values of \(F_{21}\), \(A_1\), and \(A_2\)

Now, we can substitute the available values of \(F_{21}\), \(A_1\), and \(A_2\) into the equation to find the value of \(F_{12}\). Note: Ensure the values of \(F_{21}\), \(A_1\), and \(A_2\) given in the problem statement are substituted in the equation.

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Most popular questions from this chapter

In a natural gas-fired boiler, combustion gases pass through 6-m-long,15-cm- diameter tubes immersed in water at \(1 \mathrm{~atm}\) pressure. The tube temperature is measured to be \(105^{\circ} \mathrm{C}\), and the emissivity of the inner surfaces of the tubes is estimated to be \(0.9\). Combustion gases enter the tube at \(1 \mathrm{~atm}\) and \(1000 \mathrm{~K}\) at a mean velocity of \(3 \mathrm{~m} / \mathrm{s}\). The mole fractions of \(\mathrm{CO}_{2}\) and \(\mathrm{H}_{2} \mathrm{O}\) in combustion gases are 8 percent and 16 percent, respectively. Assuming fully developed flow and using properties of air for combustion gases, determine \((a)\) the rates of heat transfer by convection and by radiation from the combustion gases to the tube wall and \((b)\) the rate of evaporation of water.

Determine the view factors from the base of a cube to each of the other five surfaces.

Consider two infinitely long concentric cylinders with diameters 20 and $25 \mathrm{~cm}\(. The inner surface is maintained at \)700 \mathrm{~K}$ and has an emissivity of \(0.40\), while the outer surface is black. If the rate of radiation heat transfer from the inner surface to the outer surface is $2400 \mathrm{~W}$ per unit area of the inner surface, the temperature of the outer surface is (a) \(605 \mathrm{~K}\) (b) \(538 \mathrm{~K}\) (c) \(517 \mathrm{~K}\) (d) \(451 \mathrm{~K}\) (e) \(415 \mathrm{~K}\)

Two gray surfaces that form an enclosure exchange heat with one another by thermal radiation. Surface 1 has a temperature of \(400 \mathrm{~K}\), an area of \(0.2 \mathrm{~m}^{2}\), and a total emissivity of \(0.4\). Surface 2 has a temperature of \(600 \mathrm{~K}\), an area of \(0.3 \mathrm{~m}^{2}\), and a total emissivity of \(0.6\). If the view factor \(F_{12}\) is \(0.3\), the rate of radiation heat transfer between the two surfaces is (a) \(135 \mathrm{~W}\) (b) \(223 \mathrm{~W}\) (c) \(296 \mathrm{~W}\) (d) \(342 \mathrm{~W}\) (e) \(422 \mathrm{~W}\)

=Consider a vertical 2 -m-diameter cylindrical furnace whose surfaces closely approximate black surfaces. The base, top, and side surfaces of the furnace are maintained at \(400 \mathrm{~K}, 600 \mathrm{~K}\), and \(1200 \mathrm{~K}\), respectively. If the view factor from the base surface to the top surface is \(0.2\), the net radiation heat transfer between the base and the side surfaces is (a) \(73 \mathrm{~kW}\) (b) \(126 \mathrm{~kW}\) (c) \(215 \mathrm{~kW}\) (d) \(292 \mathrm{~kW}\) (e) \(344 \mathrm{~kW}\)

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