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A spherical communication satellite with a diameter of \(2.5 \mathrm{~m}\) is orbiting the earth. The outer surface of the satellite in space has an emissivity of \(0.75\) and a solar absorptivity of \(0.10\), while solar radiation is incident on the spacecraft at a rate of $1000 \mathrm{~W} / \mathrm{m}^{2}$. If the satellite is made of material with an average thermal conductivity of \(5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and the midpoint temperature is \(0^{\circ} \mathrm{C}\), determine the heat generation rate and the surface temperature of the satellite.

Short Answer

Expert verified
The heat generation rate of the satellite is 1101.31 W, and the surface temperature is 17.58°C.

Step by step solution

01

Determine the surface area of the sphere

We can determine the surface area of the spherical satellite using its diameter, which is given as \(2.5 \mathrm{~m}\). The radius of the sphere is half the diameter, so \(r = \frac{2.5}{2} = 1.25 \mathrm{~m}\). The surface area of a sphere can be calculated as: \(A = 4 \pi r^2\) Now substitute the value of r: \(A = 4 \pi (1.25)^2 = 19.63 \mathrm{~m}^2\)
02

Calculate the absorbed solar radiation

The satellite absorbs solar radiation at a rate of \(1000 \mathrm{~W} / \mathrm{m}^2\), and its solar absorptivity is \(0.10\). To find the total absorbed solar radiation, we can multiply the satellite's surface area by the rate of solar radiation and the absorptivity: \(Q_{in} = A \cdot S \cdot \alpha\) where \(Q_{in}\) is the absorbed solar radiation, \(A\) is the surface area, \(S\) is the incident solar radiation, and \(\alpha\) is the solar absorptivity. Now substitute the values: \(Q_{in} = 19.63 \cdot 1000 \cdot 0.10 = 1963 \mathrm{~W}\)
03

Calculate the emitted thermal radiation

The satellite emits thermal radiation due to its emissivity, which is given as \(0.75\). The equation for the emitted thermal radiation is: \(Q_{out} = \epsilon \cdot A \cdot \sigma \cdot T^4\) where \(Q_{out}\) is the emitted thermal radiation, \(\epsilon\) is the emissivity, \(\sigma\) is the Stefan-Boltzmann constant \((5.67 \times 10^{-8} \mathrm{~W} / \mathrm{m}^2 \cdot \mathrm{K}^4)\), and \(T\) is the temperature in Kelvin. First, we need to convert the midpoint temperature from Celsius to Kelvin: \(T = 0^{\circ} \mathrm{C} + 273.15 = 273.15 \mathrm{~K}\) Now substitute the values into the equation: \(Q_{out} = 0.75 \cdot 19.63 \cdot 5.67 \times 10^{-8} \cdot (273.15)^4 = 861.69 \mathrm{~W}\)
04

Determine the heat generation rate

The heat generation rate (\(Q_{gen}\)) can be determined by the difference between the absorbed solar radiation and the emitted thermal radiation: \(Q_{gen} = Q_{in} - Q_{out}\) Substitute the values: \(Q_{gen} = 1963 - 861.69 = 1101.31 \mathrm{~W}\)
05

Calculate the surface temperature

To find the surface temperature, we can use the following equation: \(T_{surface} = T + \frac{Q_{gen}}{4 \pi r k}\) where \(T_{surface}\) is the surface temperature, \(T\) is the satellite's midpoint temperature, \(r\) is the radius, and \(k\) is the average thermal conductivity. Now substitute the values: \(T_{surface} = 273.15 + \frac{1101.31}{4 \pi (1.25) 5} = 273.15 + 17.58 = 290.73 \mathrm{~K}\) Finally, convert the surface temperature from Kelvin to Celsius: \(T_{surface}^{\circ} \mathrm{C} = 290.73 - 273.15 = 17.58^{\circ} \mathrm{C}\) In conclusion, the heat generation rate of the satellite is \(1101.31 \mathrm{~W}\), and the surface temperature is \(17.58^{\circ} \mathrm{C}\).

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Most popular questions from this chapter

The variation of temperature in a plane wall is determined to be $T(x)=65 x+25\( where \)x\( is in \)\mathrm{m}\( and \)T\( is in \){ }^{\circ} \mathrm{C}$. If the temperature at one surface is \(38^{\circ} \mathrm{C}\), the thickness of the wall is (a) \(2 \mathrm{~m}\) (b) \(0.4 \mathrm{~m}\) (c) \(0.2 \mathrm{~m}\) (d) \(0.1 \mathrm{~m}\) (e) \(0.05 \mathrm{~m}\)

A spherical container with an inner radius \(r_{1}=1 \mathrm{~m}\) and an outer radius \(r_{2}=1.05 \mathrm{~m}\) has its inner surface subjected to a uniform heat flux of \(\dot{q}_{1}=7 \mathrm{~kW} / \mathrm{m}^{2}\). The outer surface of the container has a temperature \(T_{2}=25^{\circ} \mathrm{C}\), and the container wall thermal conductivity is $k=1.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. Show that the variation of temperature in the container wall can be expressed as $T(r)=\left(\dot{q}_{1} r_{1}^{2} / k\right)\left(1 / r-1 / r_{2}\right)+T_{2}$ and determine the temperature of the inner surface of the container at \(r=r_{1}\).

Is the thermal conductivity of a medium, in general, constant or does it vary with temperature?

In metal processing plants, workers often operate near hot metal surfaces. Exposed hot surfaces are hazards that can potentially cause thermal burns on human skin. Metallic surfaces above \(70^{\circ} \mathrm{C}\) are considered extremely hot. Damage to skin can occur instantaneously upon contact with metallic surfaces at that temperature. In a plant that processes metal plates, a plate is conveyed through a series of fans to cool its surface in an ambient temperature of \(30^{\circ} \mathrm{C}\). The plate is \(25 \mathrm{~mm}\) thick and has a thermal conductivity of $13.5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. The temperature at the bottom surface of the plate is monitored by an infrared (IR) thermometer. Obtain an expression for the variation of temperature in the metal plate. The IR thermometer measures the bottom surface of the plate to be \(60^{\circ} \mathrm{C}\). Determine the minimum value of the convection heat transfer coefficient needed to keep the top surface below \(47^{\circ} \mathrm{C}\).

Consider a large plane wall of thickness \(L=0.3 \mathrm{~m}\), thermal conductivity \(k=2.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and surface area \(A=12 \mathrm{~m}^{2}\). The left side of the wall at \(x=0\) is subjected to a net heat flux of \(\dot{q}_{0}=700 \mathrm{~W} / \mathrm{m}^{2}\), while the temperature at that surface is measured to be $T_{1}=80^{\circ} \mathrm{C}$. Assuming constant thermal conductivity and no heat generation in the wall, \((a)\) express the differential equation and the boundary conditions for steady one-dimensional heat conduction through the wall, \((b)\) obtain a relation for the variation of temperature in the wall by solving the differential equation, and ( \(c\) ) evaluate the temperature of the right surface of the wall at \(x=L\). Answer: (c) \(-4^{\circ} \mathrm{C}\)

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