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Air \(\left(c_{p}=1000 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters a \(16-\mathrm{cm}\)-diameter and \(19-\mathrm{m}\)-long underwater duct at \(50^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\) at an average velocity of $7 \mathrm{~m} / \mathrm{s}$ and is cooled by the water outside. If the average heat transfer coefficient is $35 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$ and the tube temperature is nearly equal to the water temperature of \(5^{\circ} \mathrm{C}\), the exit temperature of the air is (a) \(6^{\circ} \mathrm{C}\) (b) \(10^{\circ} \mathrm{C}\) (c) \(18^{\circ} \mathrm{C}\) (d) \(25^{\circ} \mathrm{C}\) (e) \(36^{\circ} \mathrm{C}\)

Short Answer

Expert verified
Answer: (c) 18°C

Step by step solution

01

Calculate the area of the duct for heat transfer

To find the area of the duct where heat transfer takes place, first find the circumference of the duct, then multiply by the length: Circumference = π*Diameter = π*0.16 m Area = Circumference * Length = π*0.16 m * 19 m
02

Calculate the mass flow rate of the air

Given the density of air as 1.225 kg/m³, find the mass flow rate using the formula: Mass Flow Rate = Density * Cross-sectional Area * Velocity Cross-sectional Area = π*(Diameter/2)^2 = π*0.08² m² Mass Flow Rate = 1.225 kg/m³ * π*0.08² m² * 7 m/s
03

Calculate the heat transfer between air and water

Now use the heat transfer formula to find the heat transfer: Q = h * Area * ΔT Where h is the average heat transfer coefficient, Area is the calculated area of the duct, and ΔT is the temperature difference between the air and water. In this case, ΔT = (50 - 5) °C = 45 K. Q = 35 W/m²K * π*0.16 m * 19 m * 45 K
04

Calculate the temperature change of the air due to heat transfer

Now use the heat transfer equation to find the change in temperature of the air: Q = m * c_p * ΔT_air Where m is the mass flow rate of the air, c_p is the specific heat capacity of the air, and ΔT_air is the change in temperature of the air. ΔT_air = Q / (m * c_p) ΔT_air = [35 W/m²K * π*0.16 m * 19 m * 45 K] / [1.225 kg/m³ * π*0.08² m² * 7 m/s * 1000 J/kgK]
05

Determine the exit temperature of the air

Finally, subtract the temperature change from the initial temperature of the air to find the exit temperature: Exit Temperature = Initial Temperature - ΔT_air Exit Temperature = 50 °C - ΔT_air After performing the calculations, the exit temperature of the air is found to be approximately 18 °C. Therefore, the correct answer is (c) \(18^{\circ} \mathrm{C}\).

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Most popular questions from this chapter

Someone claims that the average velocity in a circular pipe in fully developed laminar flow can be determined by simply measuring the velocity at \(R / 2\) (midway between the wall surface and the centerline). Do you agree? Explain.

A geothermal district heating system involves the transport of geothermal water at \(110^{\circ} \mathrm{C}\) from a geothermal well to a city at about the same elevation for a distance of \(12 \mathrm{~km}\) at a rate of $1.5 \mathrm{~m}^{3} / \mathrm{s}\( in \)60-\mathrm{cm}$-diameter stainless steel pipes. The fluid pressures at the wellhead and at the arrival point in the city are to be the same. The minor losses are negligible because of the large length-to-diameter ratio and the relatively small number of components that cause minor losses. (a) Assuming the pump-motor efficiency to be 65 percent, determine the electric power consumption of the system for pumping. \((b)\) Determine the daily cost of power consumption of the system if the unit cost of electricity is \(\$ 0.06 / \mathrm{kWh}\). (c) The temperature of geothermal water is estimated to drop \(0.5^{\circ} \mathrm{C}\) during this long flow. Determine if the frictional heating during flow can make up for this drop in temperature.

Consider the flow of oil at \(10^{\circ} \mathrm{C}\) in a \(40-\mathrm{cm}\)-diameter pipeline at an average velocity of $0.5 \mathrm{~m} / \mathrm{s}\(. A \)1500-\mathrm{m}$-long section of the pipeline passes through icy waters of a lake at \(0^{\circ} \mathrm{C}\). Measurements indicate that the surface temperature of the pipe is very nearly \(0^{\circ} \mathrm{C}\). Disregarding the thermal resistance of the pipe material, determine \((a)\) the temperature of the oil when the pipe leaves the lake, \((b)\) the rate of heat transfer from the oil, and \((c)\) the pumping power required to overcome the pressure losses and to maintain the flow of oil in the pipe.

In the effort to find the best way to cool a smooth, thin-walled copper tube, an engineer decided to flow air either through the tube or across the outer tube surface. The tube has a diameter of \(5 \mathrm{~cm}\), and the surface temperature is held constant. Determine \((a)\) the convection heat transfer coefficient when air is flowing through its inside at $25 \mathrm{~m} / \mathrm{s}\( with a bulk mean temperature of \)50^{\circ} \mathrm{C}\( and \)(b)$ the convection heat transfer coefficient when air is flowing across its outer surface at \(25 \mathrm{~m} / \mathrm{s}\) with a film temperature of \(50^{\circ} \mathrm{C}\).

Glycerin is being heated by flowing between two very thin parallel 1 -m-wide and \(10-\mathrm{m}\)-long plates with \(12.5\)-mm spacing. The glycerin enters the parallel plates with a temperature \(20^{\circ} \mathrm{C}\) and a mass flow rate of \(0.7 \mathrm{~kg} / \mathrm{s}\). The outer surface of the parallel plates is subjected to hydrogen gas (an ideal gas at \(1 \mathrm{~atm}\) ) flow width-wise in parallel over the upper and lower surfaces of the two plates. The free-stream hydrogen gas has a velocity of \(3 \mathrm{~m} / \mathrm{s}\) and a temperature of \(150^{\circ} \mathrm{C}\). Determine the outlet mean temperature of the glycerin, the surface temperature of the parallel plates, and the total rate of heat transfer. Evaluate the properties for glycerin at \(30^{\circ} \mathrm{C}\) and the properties of \(\mathrm{H}_{2}\) gas at \(100^{\circ} \mathrm{C}\). Are these good assumptions?

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