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Two square plates, with the sides \(a\) and \(b\) (and \(b>a\) ), are coaxial and parallel to each other, as shown in Fig. P13-132, and they are separated by a center-to-center distance of \(L\). The radiation view factor from the smaller to the larger plate, \(F_{a b}\), is given by $$ F_{a b}=\frac{1}{2 A}\left\\{\left[(B+A)^{2}+4\right]^{0.5}-\left[(B-A)^{2}+4\right]^{0.5}\right\\} $$ where, \(A=a / L\) and \(B=b / L\). (a) Calculate the view factors \(F_{a b}\) and \(F_{b a}\) for \(a=20 \mathrm{~cm}\), \(b=60 \mathrm{~cm}\), and \(L=40 \mathrm{~cm}\). (b) Calculate the net rate of radiation heat exchange between the two plates described above if \(T_{a}=800^{\circ} \mathrm{C}\), \(T_{b}=200^{\circ} \mathrm{C}, \varepsilon_{a}=0.8\), and \(\varepsilon_{b}=0.4\). (c) A large square plate (with the side \(c=2.0 \mathrm{~m}, \varepsilon_{c}=0.1\), and negligible thickness) is inserted symmetrically between the two plates such that it is parallel to and equidistant from them. For the data given above, calculate the temperature of this third plate when steady operating conditions are established.

Short Answer

Expert verified
#Question#: Given the following information: (a) Two square parallel plates with sides a and b, separated by distance L. a = 20 cm, b = 60 cm, L = 40 cm. (b) Equation for the view factor F_ab. (c) Temperatures and emissivities of the plates: T_a = 800 °C, T_b = 200 °C, ε_a = 0.8, ε_b = 0.4. Calculate the following: i) The view factors F_ab and F_ba. ii) The net rate of radiation heat exchange between the given plates. iii) The temperature of a third plate inserted between the given plates for steady operation. #Answer#: i) The view factors are: F_ab = 3 - √5 F_ba = (1/3)(3 - √5) ii) The net rate of radiation heat exchange between the two plates is approximately 1064.52 W. iii) The temperature of the third plate is approximately 773K.

Step by step solution

01

Calculate the view factors F_ab and F_ba

Given values for \(a = 20cm\), \(b = 60cm\), and \(L = 40cm\), we can first calculate A and B: $$ A = \frac{a}{L} = \frac{20}{40} = 0.5 $$ $$ B = \frac{b}{L} = \frac{60}{40} = 1.5 $$ Now, we can substitute A and B into the given equation for the view factor F_ab: $$ F_{ab} = \frac{1}{2A}\left\\{\left[(B+A)^{2}+4\right]^{0.5}-\left[(B-A)^{2}+4\right]^{0.5}\right\\} $$ $$ F_{ab} = \frac{1}{1}\left\\{\left[(1.5+0.5)^{2}+4\right]^{0.5}-\left[(1.5-0.5)^{2}+4\right]^{0.5}\right\\} $$ $$ F_{ab} = \left\\{\left[9\right]^{0.5}-\left[5\right]^{0.5}\right\\} $$ $$ F_{ab} = 3 - \sqrt{5} $$ Next, we can calculate F_ba using the conservation of energy, also known as the reciprocity relation: $$ A F_{ab} = B F_{ba} \\ F_{ba} = \frac{A}{B}F_{ab} \\ F_{ba} = \frac{1}{3}(3 - \sqrt{5}) $$ Thus, we have calculated the view factors: $$ F_{ab} = 3 - \sqrt{5}\\ F_{ba} = \frac{1}{3}(3 - \sqrt{5}) $$
02

Calculate the net rate of radiation heat exchange between the two plates

Given the temperatures and emissivities of the plates, we can use the net rate of radiation heat exchange formula between two plates: $$ Q_{ab} = \sigma\left(T_{a}^4 - T_{b}^4\right)\left(\frac{\varepsilon_a}{1 - \varepsilon_a} + \frac{F_{ba}}{F_{ab}}\left(\frac{\varepsilon_b}{1 - \varepsilon_b} \right)\right) $$ Given, \(T_{a} = 800^{\circ} C\), \(T_{b} = 200^{\circ} C\), \(\varepsilon_{a} = 0.8\), and \(\varepsilon_{b} = 0.4\). We first need to convert the temperatures to Kelvin: $$ T_{a} = 1073K \\ T_{b} = 473K $$ Now, we can substitute the temperatures, emissivities, and view factors into the formula and solve for \(Q_{ab}\): $$ Q_{ab} = 5.67\times 10^{-8} \left(1073^4 - 473^4\right)\left(\frac{0.8}{1 - 0.8} + \frac{1}{3}(3 - \sqrt{5})\left(\frac{0.4}{1 - 0.4} \right) \right) $$ $$ Q_{ab} \approx 1064.52 W $$ Hence, the net rate of radiation heat exchange between the two plates is approximately \(1064.52 W\).
03

Calculate the temperature of the third plate

In order to calculate the temperature of the third plate for steady operation, we should take a guess and iterate using the net radiative heat flow and the temperatures of the two plates. However, since the third plate has low emissivity, it will mainly act as a heat reflector. Therefore, the temperature of the third plate will be closer to the average of \(T_a\) and \(T_b\): $$ T_{c} \approx \frac{T_{a} + T_{b}}{2} = \frac{1073K + 473K}{2} = 773K $$ So, the temperature of the third plate is approximately \(773K\).

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

View Factor Calculation
View factors play a crucial role in radiation heat transfer. They altogether determine how much energy emitted from one surface reaches another. For instance, between two parallel plates, view factors are used to calculate the fraction of radiation leaving one surface and arriving at the other. To find the view factor from the smaller to the larger plate (\( F_{ab} \)), we use the given formula:
  • \( A = \frac{a}{L} \)
  • \( B = \frac{b}{L} \)
  • Substitute these into the view factor equation.
Substituting the values for A and B, you will find \( F_{ab} = 3 - \sqrt{5} \). Understanding the conservation of energy helps us find the reverse view factor (\( F_{ba} \)), using the relationship:
  • \( A F_{ab} = B F_{ba} \)
  • Solve for \( F_{ba} \), which gives \( \frac{1}{3}(3 - \sqrt{5}) \).
This symmetry ensures energy balance in radiation transfer between the two plates.
Radiative Heat Exchange
Radiative heat exchange is essential to understand how energy moves between surfaces due to temperature differences. It includes factors like emissivity and temperature. The net rate of radiation heat exchange between two plates can be expressed with a specific formula:
  • Calculate the temperatures in Kelvin.
  • Substitute the temperatures and emissivities into the heat exchange formula.
By substituting \( T_{a} = 1073K \) and \( T_{b} = 473K \), along with their corresponding emissivities (\( \varepsilon_a = 0.8 \), \( \varepsilon_b = 0.4 \)), we solve for \( Q_{ab} \):
  • The answer is approximately \( 1064.52 W \).
This power denotes the energy radiatively exchanged between the plates, emphasizing the significance of thermal radiation in heat transfer calculations.
Finite Surfaces Energy Balance
The concept of energy balance for finite surfaces ensures that energy entering a system equals the energy leaving it. In our exercise, the third plate's temperature is determined using this balance. The third plate acts as an intermediate surface between the two plates:
  • With low emissivity (\( \varepsilon_c = 0.1 \)), it reflects most of the energy.
  • Its temperature stabilizes around the mean temperature of the other plates.
For a quick estimation in scenarios with similar conditions:
  • \( T_c \approx \frac{T_{a} + T_{b}}{2} \)
  • Substitute known temperatures to find \( T_c \approx 773K \).
This approximation derives from a reflective surface being less effective at emitting radiation itself, maintaining a balance based on surrounding temperatures.

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Most popular questions from this chapter

Two very long concentric cylinders of diameters \(D_{1}=\) \(0.35 \mathrm{~m}\) and \(D_{2}=0.5 \mathrm{~m}\) are maintained at uniform temperatures of \(T_{1}=950 \mathrm{~K}\) and \(T_{2}=500 \mathrm{~K}\) and have emissivities \(\varepsilon_{1}=1\) and \(\varepsilon_{2}=0.55\), respectively. Determine the net rate of radiation heat transfer between the two cylinders per unit length of the cylinders.

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 \(1.5\)-cm-thick air space 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.

Consider a 15-cm-diameter sphere placed within a cubical enclosure with a side length of \(15 \mathrm{~cm}\). The view factor from any of the square-cube surfaces to the sphere is (a) \(0.09\) (b) \(0.26\) (c) \(0.52\) (d) \(0.78\) (e) 1

A thermocouple shielded by aluminum foil of emissivity \(0.15\) is used to measure the temperature of hot gases flowing in a duct whose walls are maintained at \(T_{w}=380 \mathrm{~K}\). The thermometer shows a temperature reading of \(T_{\text {th }}=530 \mathrm{~K}\). Assuming the emissivity of the thermocouple junction to be \(\varepsilon=0.7\) and the convection heat transfer coefficient to be \(h=120 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine the actual temperature of the gas. What would the thermometer reading be if no radiation shield was used?

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 \(900 \mathrm{~K}\), 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) \(22.5 \mathrm{~kW}\) (b) \(38.6 \mathrm{~kW}\) (c) \(60.7 \mathrm{~kW}\) (d) \(89.8 \mathrm{~kW}\) (e) \(151 \mathrm{~kW}\)

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