A 1-m-inner-diameter liquid-oxygen storage tank at a hospital keeps the liquid oxygen at \(90 \mathrm{~K}\). The tank consists of a \(0.5-\mathrm{cm}\)-thick aluminum ( \(k=170 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) shell whose exterior is covered with a 10 -cm-thick layer of insulation \((k=\) \(0.02 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\). The insulation is exposed to the ambient air at \(20^{\circ} \mathrm{C}\) and the heat transfer coefficient on the exterior side of the insulation is \(5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The temperature of the exterior surface of the insulation is (a) \(13^{\circ} \mathrm{C}\) (b) \(9^{\circ} \mathrm{C}\) (c) \(2^{\circ} \mathrm{C}\) (d) \(-3^{\circ} \mathrm{C}\) (e) \(-12^{\circ} \mathrm{C}\)

Short Answer

Expert verified
Solution: Calculate the overall conduction resistance - Calculate Aluminum Resistance - Calculate Insulation Resistance - Compute Overall Resistance Perform energy balance with convection resistance - Compute Convection Resistance - Perform Heat Energy Balance Solve for the exterior surface temperature - Rearrange Energy Balance Equation - Calculate Exterior Surface Temperature Result: Verify which option is closest to the obtained value: (a) \(13^{\circ} \mathrm{C}\) (b) \(9^{\circ} \mathrm{C}\) (c) \(2^{\circ} \mathrm{C}\) (d) \(-3^{\circ} \mathrm{C}\) (e) \(-12^{\circ} \mathrm{C}\)

Step by step solution

01

Calculate Aluminum Resistance

Using the formula for the resistance of a cylinder, calculate the resistance through the aluminum shell: \(R_{al} = \frac{ln(r_2/r_1)}{2 \pi \; l \; k_{al}}\) Where: \(r_1\) is the inner radius of the aluminum shell (0.5 m) \(r_2\) is the outer radius of the aluminum shell (0.5 m + 0.005 m) \(l\) is the length of the aluminum shell (1 m) \(k_{al}\) is the thermal conductivity of the aluminum (170 W/m⋅K)
02

Calculate Insulation Resistance

Calculate the resistance through the insulation: \(R_{ins} = \frac{ln(r_3/r_2)}{2 \pi \; l \; k_{ins}}\) Where: \(r_3\) is the outer radius of the insulation (0.5 m + 0.005 m + 0.1 m) \(k_{ins}\) is the thermal conductivity of the insulation (0.02 W/m⋅K)
03

Compute Overall Resistance

Calculate the overall conduction resistance: \(R_{cond} = R_{al} + R_{ins}\) Step 2: Perform energy balance with convection resistance
04

Compute Convection Resistance

Calculate the convection resistance on the exterior side of the insulation: \(R_{conv} = \frac{1}{h \; A}\) Where: \(h\) is the heat transfer coefficient (5 W/m²⋅K) \(A\) is the surface area of the exterior side of the insulation (\(2 \pi \; r_3 \; l\))
05

Heat Energy Balance

Perform a heat energy balance by equating the heat transfer rate through conduction and convection: \(Q = \frac{T_{ins} - T_{liq}}{R_{cond}} = \frac{T_{amb} - T_{ins}}{R_{conv}}\) Where: \(T_{liq}\) is the temperature of the liquid oxygen (90 K or -183.15°C) \(T_{ins}\) is the temperature of the exterior surface of the insulation (unknown) \(T_{amb}\) is the ambient temperature (20°C) Step 3: Solve for the exterior surface temperature
06

Rearrange Energy Balance Equation

Rearrange the heat energy balance equation to solve for the exterior surface temperature: \(T_{ins} = \frac{T_{liq} \; R_{conv} + T_{amb} \; R_{cond}}{R_{conv} + R_{cond}}\)
07

Calculate Exterior Surface Temperature

Calculate the exterior surface temperature of the insulation: \(T_{ins} = \frac{(-183.15 \mathrm{~°C}) \; R_{conv} + (20 \mathrm{~°C}) \; R_{cond}}{R_{conv} + R_{cond}}\) Once we calculated \(T_{ins}\), we can verify which one of the given options is closest to the obtained value: (a) \(13^{\circ} \mathrm{C}\) (b) \(9^{\circ} \mathrm{C}\) (c) \(2^{\circ} \mathrm{C}\) (d) \(-3^{\circ} \mathrm{C}\) (e) \(-12^{\circ} \mathrm{C}\)

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Most popular questions from this chapter

The boiling temperature of nitrogen at atmospheric pressure at sea level ( 1 atm pressure) is \(-196^{\circ} \mathrm{C}\). Therefore, nitrogen is commonly used in low-temperature scientific studies since the temperature of liquid nitrogen in a tank open to the atmosphere will remain constant at \(-196^{\circ} \mathrm{C}\) until it is depleted. Any heat transfer to the tank will result in the evaporation of some liquid nitrogen, which has a heat of vaporization of \(198 \mathrm{~kJ} / \mathrm{kg}\) and a density of \(810 \mathrm{~kg} / \mathrm{m}^{3}\) at 1 atm. Consider a 3-m-diameter spherical tank that is initially filled with liquid nitrogen at 1 atm and \(-196^{\circ} \mathrm{C}\). The tank is exposed to ambient air at \(15^{\circ} \mathrm{C}\), with a combined convection and radiation heat transfer coefficient of \(35 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The temperature of the thin-shelled spherical tank is observed to be almost the same as the temperature of the nitrogen inside. Determine the rate of evaporation of the liquid nitrogen in the tank as a result of the heat transfer from the ambient air if the tank is \((a)\) not insulated, \((b)\) insulated with 5 -cm-thick fiberglass insulation \((k=0.035 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\), and (c) insulated with 2 -cm-thick superinsulation which has an effective thermal conductivity of \(0.00005 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\).

Consider a 25-m-long thick-walled concrete duct \((k=\) \(0.75 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) of square cross section. The outer dimensions of the duct are \(20 \mathrm{~cm} \times 20 \mathrm{~cm}\), and the thickness of the duct wall is \(2 \mathrm{~cm}\). If the inner and outer surfaces of the duct are at \(100^{\circ} \mathrm{C}\) and \(30^{\circ} \mathrm{C}\), respectively, determine the rate of heat transfer through the walls of the duct. Answer: \(47.1 \mathrm{~kW}\)

Consider a house whose attic space is ventilated effectively so that the air temperature in the attic is the same as the ambient air temperature at all times. Will the roof still have any effect on heat transfer through the ceiling? Explain.

Two finned surfaces are identical, except that the convection heat transfer coefficient of one of them is twice that of the other. For which finned surface is the \((a)\) fin effectiveness and \((b)\) fin efficiency higher? Explain.

A 1-cm-diameter, 30-cm-long fin made of aluminum \((k=237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) is attached to a surface at \(80^{\circ} \mathrm{C}\). The surface is exposed to ambient air at \(22^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(11 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). If the fin can be assumed to bery long, its efficiency is (a) \(0.60\) (b) \(0.67\) (c) \(0.72\) (d) \(0.77\) (e) \(0.88\)

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