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A spherical tank with an inner diameter of \(3 \mathrm{~m}\) is filled with a solution undergoing an exothermic reaction that generates $233 \mathrm{~W} / \mathrm{m}^{3}\( of heat and causes the surface temperature to be \)120^{\circ} \mathrm{C}$. To prevent thermal burn hazards, the tank is enclosed by a concentric outer cover that provides an air gap of \(5 \mathrm{~cm}\) in the enclosure. Determine whether the air gap is sufficient to keep the outer cover temperature below \(45^{\circ} \mathrm{C}\) to prevent thermal burns on human skin. Evaluate the properties of air in the enclosure at $80^{\circ} \mathrm{C}$ and 1 atm pressure. Is this a good assumption?

Short Answer

Expert verified
Answer: Yes, the air gap is sufficient, as the calculated outer cover temperature is approximately \(37.46^{\circ}\mathrm{C}\), which is below the threshold of \(45^{\circ}\mathrm{C}\).

Step by step solution

01

Compute the heat generated in the tank

We are given the heat generation rate in the tank (\(233\mathrm{~W/m^3}\)) and the tank's inner diameter (\(3\mathrm{~m}\)). First, we need to find the volume of the tank. The radius of the tank (\(r_t\)) can be found using the diameter: $$r_t = \frac{d}{2} = \frac{3\mathrm{~m}}{2}=1.5\mathrm{~m}$$ Now we can find the volume of the tank (\(V_t\)) using the formula for the volume of a sphere: $$V_t = \frac{4}{3}\pi r_t^3 = \frac{4}{3}\pi (1.5\mathrm{~m})^3 \approx 14.137\mathrm{~m^3}$$ Next, we can calculate the total heat generated in the tank (\(q_t\)) using the heat generation rate: $$q_t = \left( 233\frac{\mathrm{W}}{\mathrm{m}^3} \right) \times \left( 14.137\mathrm{~m^3} \right) \approx 3293.99\mathrm{~W}$$
02

Calculate the heat transfer through the air gap

To do this, we first find the thermal resistance (\(R_{airgap}\)) of the air gap using the formula for the thermal resistance of a concentric sphere: $$R_{airgap} = \frac{1}{4\pi k_{air} }\left( \frac{1}{r_t}-\frac{1}{r_{cover}} \right)$$ Here, \(k_{air}\) is the thermal conductivity of the air in the gap (evaluated at \(80^{\circ}\mathrm{C}\)), \(r_t\) is the radius of the tank (\(1.5\mathrm{~m}\)), and \(r_{cover}\) is the radius of the outer cover. The air gap is \(5\mathrm{~cm}\) or \(0.05\mathrm{~m}\), so the radius of the outer cover is: $$r_{cover}=r_t + 0.05\mathrm{~m} = 1.55\mathrm{~m}$$ Given that we're evaluating the properties of air in the enclosure at \(80^{\circ}\mathrm{C}\), the thermal conductivity of air (\(k_{air}\)) can be found in the literature or using an online calculator. We'll assume \(k_{air} \approx 0.0342\mathrm{~W/(m\cdot K)}\). Now we can find the thermal resistance of the air gap: $$R_{airgap} = \frac{1}{4\pi(0.0342\mathrm{~W/(m\cdot K)}) }\left( \frac{1}{1.5\mathrm{~m}}-\frac{1}{1.55\mathrm{~m}} \right) \approx 4.052\mathrm{~m^2 \cdot K/W}$$ Since the heat generated in the tank must transfer through the air gap, we can use the thermal resistance to find the heat transfer through the air gap: $$q_{airgap} = \frac{T_t-T_{cover}}{R_{airgap}}$$ Here, \(T_t\) is the surface temperature of the tank, which is given as \(120^{\circ}\mathrm{C}\), and \(T_{cover}\) is the temperature of the outer cover, which we want to find.
03

Determine the temperature of the outer cover

Now we can solve for \(T_{cover}\) using the equation above: $$T_{cover} = T_t - q_{airgap}\cdot R_{airgap} = 120^{\circ}\mathrm{C} - (3293.99\mathrm{~W}) \times (4.052\mathrm{~m^2 \cdot K/W}) \approx 37.46^{\circ}\mathrm{C}$$
04

Check the assumption for air properties

Since the temperature of the outer cover is calculated as \(37.46^{\circ}\mathrm{C}\), which is close to the given temperature of air at \(80^{\circ}\mathrm{C}\), our assumption of using the properties of air at this temperature is appropriate. Since the outer cover temperature is \(37.46^{\circ}\mathrm{C}\), which is below the threshold of \(45^{\circ}\mathrm{C}\), we can conclude that the air gap is sufficient to keep the outer cover temperature below the threshold and prevent thermal burns.

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Most popular questions from this chapter

Flat-plate solar collectors are often tilted up toward the sun in order to intercept a greater amount of direct solar radiation. The tilt angle from the horizontal also affects the rate of heat loss from the collector. Consider a \(1.5-\mathrm{m}\)-high and 3-m-wide solar collector that is tilted at an angle \(\theta\) from the horizontal. The back side of the absorber is heavily insulated. The absorber plate and the glass cover, which are spaced $2.5 \mathrm{~cm}\( from each other, are maintained at temperatures of \)80^{\circ} \mathrm{C}\( and \)40^{\circ} \mathrm{C}$, respectively. Determine the rate of heat loss from the absorber plate by natural convection for $\theta=0^{\circ}, 30^{\circ}\(, and \)90^{\circ}$.

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Hot water is flowing at an average velocity of \(4 \mathrm{ft} / \mathrm{s}\) through a cast iron pipe $\left(k=30 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}\right)$ whose inner and outer diameters are \(1.0\) in and \(1.2\) in, respectively. The pipe passes through a 50 -ft-long section of a basement whose temperature is $60^{\circ} \mathrm{F}\(. The emissivity of the outer surface of the pipe is \)0.5$, and the walls of the basement are also at about \(60^{\circ} \mathrm{F}\). If the inlet temperature of the water is \(150^{\circ} \mathrm{F}\) and the heat transfer coefficient on the inner surface of the pipe is $30 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}$, determine the temperature drop of water as it passes through the basement. Evaluate air properties at a film temperature of \(105^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\) pressure. Is this a good assumption?

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