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Water is to be heated from \(10^{\circ} \mathrm{C}\) to \(80^{\circ} \mathrm{C}\) as it flows through a \(2-\mathrm{cm}\)-internal-diameter, \(13-\mathrm{m}\)-long tube. The tube is equipped with an electric resistance heater, which provides uniform heating throughout the surface of the tube. The outer surface of the heater is well insulated, so in steady operation all the heat generated in the heater is transferred to the water in the tube. If the system is to provide hot water at a rate of \(5 \mathrm{~L} / \mathrm{min}\), determine the power rating of the resistance heater. Also, estimate the inner surface temperature of the pipe at the exit.

Short Answer

Expert verified
Answer: The mass flow rate of the water is 5/60 kg/s. 2. What is the heat transfer rate in kW? Answer: The heat transfer rate is 24.5 kW. 3. What is the power rating of the resistance heater? Answer: The power rating of the resistance heater is 24.5 kW. 4. What is the inner surface temperature of the pipe at the exit in °C? Answer: The inner surface temperature of the pipe at the exit is approximately 80.53 °C.

Step by step solution

01

Find the mass flow rate of the water

To find the mass flow rate of the water, we need to convert the flow rate given in Liters per minute to a mass flow rate in kg/s. We'll use the density of the water, which is typically 1000 kg/m³. Flow Rate = 5 L/min = 5/1000 m³/min = (5/1000)*(1/60) m³/s Now convert the flow rate to mass flow rate using the density of water: Mass Flow Rate = (5/1000)*(1/60) m³/s * 1000 kg/m³ = 5/60 kg/s
02

Calculate the heat transfer rate

To calculate the heat transfer rate, we can use the formula: Heat Transfer Rate = Mass Flow Rate * Specific Heat Capacity * Temperature Change where Specific Heat Capacity of water (C_p) = 4.18 kJ/kg·K Temperature Change = 80 - 10 = 70 K Heat Transfer Rate = (5/60 kg/s) * (4.18 kJ/kg·K) * 70 K = 24.5 kW
03

Determine the power rating of the resistance heater

Since all the heat generated in the heater is transferred to the water in the tube, the power rating of the resistance heater is equal to the heat transfer rate. Power Rating of Heater = Heat Transfer Rate = 24.5 kW
04

Estimate the inner surface temperature of the pipe at the exit

We can estimate the inner surface temperature of the pipe at the exit using the heat transfer rate. Let's denote the heat transfer coefficient as h and the temperature difference between the inner surface of the pipe and the exit temperature of the water as ΔT. We can use the formula: Heat Transfer Rate = h * (π * Diameter * Length) * ΔT Assuming a heat transfer coefficient (h) of 5000 W/m²·K: 24.5 kW = (5000 W/m²·K) * (π * 0.02 m * 13 m) * ΔT Solve for ΔT and add to the exit temperature of the water (80 °C): Inner Surface Temperature at Exit = ΔT + 80 = 80.53 °C The inner surface temperature of the pipe at the exit is approximately 80.53 °C. In conclusion, the power rating of the resistance heater is 24.5 kW, and the inner surface temperature of the pipe at the exit is approximately 80.53 °C.

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Most popular questions from this chapter

Liquid water flows in a thin-walled circular tube, where the pumping power required to overcome the turbulent flow pressure loss in the tube is $100 \mathrm{~W}\(. The water enters the tube at \)10^{\circ} \mathrm{C}$, where it is heated at a rate of \(3.6 \mathrm{~kW}\). The average convection heat transfer coefficient for the internal flow is $120 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. The tube is \)3 \mathrm{~m}$ long and has an inner diameter of \(12.5 \mathrm{~mm}\). The tube surface is maintained at a constant temperature. At the tube exit, an ethylene propylene diene (EPDM) rubber o-ring is attached to the tube's outer surface. The maximum temperature permitted for the o-ring is \(150^{\circ} \mathrm{C}\) (ASME Boiler and Pressure Vessel Code, BPVC. IV-2015, HG-360). Is the EPDM o-ring suitable for this operation? Evaluate the fluid properties at \(10^{\circ} \mathrm{C}\). Is this an appropriate temperature at which to evaluate the fluid properties?

Liquid water flows in a circular tube at a mass flow rate of $0.12 \mathrm{~kg} / \mathrm{s}\(. The water enters the tube at \)65^{\circ} \mathrm{C}\(, where it is heated at a rate of \)5.5 \mathrm{~kW}$. The tube is circular with a length of \(3 \mathrm{~m}\) and an inner diameter of $25 \mathrm{~mm}$. The tube surface is maintained isothermal. The inner surface of the tube is lined with polyvinylidene chloride (PVDC) lining. The recommended maximum temperature for PVDC lining is \(79^{\circ} \mathrm{C}\) (ASME Code for Process Piping, ASME B31.3-2014, Table A323.4.3). Is the PVDC lining suitable for the tube under these conditions? Evaluate the fluid properties at \(70^{\circ} \mathrm{C}\). Is this an appropriate temperature at which to evaluate the fluid properties?

An 8-m-long, uninsulated square duct of cross section $0.2 \mathrm{~m} \times 0.2 \mathrm{~m}\( and relative roughness \)10^{-3}$ passes through the attic space of a house. Hot air enters the duct at \(1 \mathrm{~atm}\) and $80^{\circ} \mathrm{C}\( at a volume flow rate of \)0.15 \mathrm{~m}^{3} / \mathrm{s}$. The duct surface is nearly isothermal at \(60^{\circ} \mathrm{C}\). Determine the rate of heat loss from the duct to the attic space and the pressure difference between the inlet and outlet sections of the duct. Evaluate air properties at a bulk mean temperature of \(80^{\circ} \mathrm{C}\). Is this a good assumption?

Air \(\left(c_{p}=1007 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters a \(17-\mathrm{cm}\)-diameter and 4-m-long tube at $65^{\circ} \mathrm{C}\( at a rate of \)0.08 \mathrm{~kg} / \mathrm{s}$ and leaves at \(15^{\circ} \mathrm{C}\). The tube is observed to be nearly isothermal at \(5^{\circ} \mathrm{C}\). The average convection heat transfer coefficient is (a) \(24.5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (b) \(46.2 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (c) \(53.9 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (d) \(67.6 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (e) \(90.7 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\)

Consider turbulent forced convection in a circular tube. Will the heat flux be higher near the inlet of the tube or near the exit? Why?

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