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A thin-walled spherical tank is buried in the ground at a depth of $3 \mathrm{~m}\(. The tank has a diameter of \)1.5 \mathrm{~m}$, and it contains chemicals undergoing exothermic reaction that provides a uniform heat flux of \(1 \mathrm{~kW} / \mathrm{m}^{2}\) to the tank's inner surface. From soil analysis, the ground has a thermal conductivity of $1.3 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\( and a temperature of \)10^{\circ} \mathrm{C}$. Determine the surface temperature of the tank. Discuss the effect of the ground depth on the surface temperature of the tank.

Short Answer

Expert verified
Answer: The surface temperature of the spherical tank is approximately -14.0606°C.

Step by step solution

01

Calculate the radius of the tank

First, let's find the radius of the spherical tank. The diameter is given as \(1.5 \mathrm{~m}\), so the radius is half of that. $$ r = \frac{1.5}{2} = 0.75 \mathrm{~m} $$
02

Calculate the area of the tank

Next, we'll find the surface area of the spherical tank. The formula for the surface area of a sphere is: $$ A = 4 \pi r^2 $$ Plug in the value for the radius: $$ A = 4 \pi (0.75)^2 = 4 \pi (0.5625) \approx 7.0686 \mathrm{~m}^2 $$
03

Calculate the total heat transfer

Now, let's find the total heat transfer from the exothermic reaction. The provided heat flux is \(1 \mathrm{~kW/m^2}\), which we need to convert to \(\mathrm{W/m^2}\) and multiply by the surface area of the tank. $$ q = 1000 \cdot A = 1000 \cdot 7.0686 = 7068.6 \mathrm{~W} $$
04

Calculate the temperature gradient

Next, we'll calculate the temperature gradient in the soil. To do this, we will use the formula for heat transfer through conduction: $$ q = -kA\frac{dT}{dx} $$ We know the heat transfer, the thermal conductivity of the soil (\(k = 1.3 \mathrm{~W/m\cdot K}\)), and the surface area of the tank. We want to find the temperature gradient, \(\frac{dT}{dx}\). Rearrange the formula to solve for \(\frac{dT}{dx}\): $$ \frac{dT}{dx} = -\frac{q}{kA} $$ Plug in the values for \(q\), \(k\), and \(A\): $$ \frac{dT}{dx} = -\frac{7068.6 \mathrm{~W}}{1.3 \mathrm{~W/m\cdot K} \cdot 7.0686 \mathrm{~m}^2} \approx -8.0202 \mathrm{~K/m} $$
05

Calculate the surface temperature of the tank

Finally, we'll find the surface temperature of the tank. We know the temperature gradient and the depth of the tank (\(3 \mathrm{~m}\)). We can find the difference in temperature by multiplying the temperature gradient by the depth of the tank: $$ \Delta T = \frac{dT}{dx} \cdot d = -8.0202 \mathrm{~K/m} \cdot 3 \mathrm{~m} \approx -24.0606 \mathrm{~K} $$ The soil temperature at the surface is given as \(10^{\circ}\mathrm{C}\). To find the surface temperature of the tank, we subtract the temperature difference from the soil temperature: $$ T_{\text{surface}} = 10 - 24.0606 \approx -14.0606^{\circ}\mathrm{C} $$
06

Conclusion

The surface temperature of the spherical tank is approximately \(-14.0606^{\circ}\mathrm{C}\). As the depth of the tank increases, the temperature gradient becomes less steep, thus the surface temperature of the tank will decrease. This means that a greater depth will result in a lower surface temperature of the tank, as it is further away from the heat source and the soil acts as an insulator.

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Most popular questions from this chapter

Liquid flows in a metal pipe with an inner diame\(D_{2}=32\) ter of $D_{1}=22 \mathrm{~mm}\( and an outer diameter of \)D_{2}=32 \mathrm{~mm}$. The thermal conductivity of the pipe wall is $12 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. The inner surface of the pipe is coated with a thin polyvinylidene chloride (PVDC) lining. Along a length of \(1 \mathrm{~m}\), the pipe outer surface is exposed to convection heat transfer with hot gas, at \(T_{\infty}=100^{\circ} \mathrm{C}\) and $h=5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(, and thermal radiation with a surrounding at \)T_{\text {surr }}=100^{\circ} \mathrm{C}\(. The emissivity at the pipe outer surface is \)0.3$. The liquid flowing inside the pipe has a convection heat transfer coefficient of \(50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). If the outer surface of the pipe is at \(85^{\circ} \mathrm{C}\), determine the temperature at the PVDC lining and the temperature of the liquid. The ASME Code for Process Piping (ASME B31.3-2014, A.323) recommends a maximum temperature for PVDC lining to be \(79^{\circ} \mathrm{C}\). Does the PVDC lining comply with the recommendation of the code?

The overall heat transfer coefficient (the \(U\)-value) of a wall under winter design conditions is \(U=2.25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Now a layer of \(100-\mathrm{mm}\) face brick is added to the outside, leaving a 20 -mm airspace between the wall and the bricks. Determine the new \(U\)-value of the wall. Also, determine the rate of heat transfer through a \(3-\mathrm{m}\)-high, 7-m-long section of the wall after modification when the indoor and outdoor temperatures are \(22^{\circ} \mathrm{C}\) and $-25^{\circ} \mathrm{C}$, respectively.

Hot- and cold-water pipes \(12 \mathrm{~m}\) long run parallel to each other in a thick concrete layer. The diameters of both pipes are \(6 \mathrm{~cm}\), and the distance between the centerlines of the pipes is \(40 \mathrm{~cm}\). The surface temperatures of the hot and cold pipes are \(60^{\circ} \mathrm{C}\) and \(15^{\circ} \mathrm{C}\), respectively. Taking the thermal conductivity of the concrete to be \(k=0.75 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), determine the rate of heat transfer between the pipes.

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Consider a \(1.5\)-m-high electric hot-water heater that has a diameter of $40 \mathrm{~cm}\( and maintains the hot water at \)60^{\circ} \mathrm{C}$. The tank is located in a small room whose average temperature is $27^{\circ} \mathrm{C}$, and the heat transfer coefficients on the inner and outer surfaces of the heater are 50 and $12 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, respectively. The tank is placed in another \(46-\mathrm{cm}\)-diameter sheet metal tank of negligible thickness, and the space between the two tanks is filled with foam insulation $(k=0.03 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$. The thermal resistances of the water tank and the outer thin sheet metal shell are very small and can be neglected. The price of electricity is \(\$ 0.08 / \mathrm{kWh}\), and the homeowner pays \(\$ 280\) a year for water heating. Determine the fraction of the hot-water energy cost of this household that is due to the heat loss from the tank. Hot-water tank insulation kits consisting of 3 -cm-thick fiberglass insulation \((k=0.035 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) large enough to wrap the entire tank are available in the market for about \(\$ 30\). If such an insulation is installed on this water tank by the homeowner himself, how long will it take for this additional insulation to pay for itself?

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