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Long cylindrical steel rods (\(\rho=7833 \mathrm{kg} / \mathrm{m}^{3}\) and \(\left.c_{p}=0.465 \mathrm{kJ} / \mathrm{kg} \cdot^{\circ} \mathrm{C}\right)\) of \(10-\mathrm{cm}\) diameter are heat treated by drawing them at a velocity of \(3 \mathrm{m} / \mathrm{min}\) through a 7 -m-long oven maintained at \(900^{\circ} \mathrm{C}\). If the rods enter the oven at \(30^{\circ} \mathrm{C}\) and leave at \(700^{\circ} \mathrm{C}\), determine ( \(a\) ) the rate of heat transfer to the rods in the oven and \((b)\) the rate of entropy generation associated with this heat transfer process.

Short Answer

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b) What is the rate of entropy generation associated with this heat transfer process?

Step by step solution

01

Calculate the mass flow rate

To calculate the mass flow rate, we need to first find the cross-sectional area and volume flow rate of the rods. The diameter of the rods is given as 10 cm, so the radius is 5 cm or 0.05 m. The cross-sectional area can be calculated using the formula for the area of a circle $$A = \pi r^2$$ Using the given radius, $$A = \pi (0.05)^2 \approx 0.007853\, \mathrm{m^²}$$ Now, we need to find the volume flow rate. The rods are moving at 3 m/min, which can be converted to m/s by dividing by 60 $$V = \frac{3\, \mathrm{m} / \mathrm{min}}{60\, \mathrm{s}} \approx 0.05\, \mathrm{m} / \mathrm{s}$$ The volume flow rate can be calculated as $$Q_{vol} = A \times V \approx 0.007853 \times 0.05 \approx 0.0003926\, \mathrm{m^3/s}$$ Finally, we can calculate the mass flow rate using the density of steel rods $$\dot{m} = \rho \times Q_{vol} \approx 7833 \times 0.0003926 \approx 3.074\, \mathrm{kg/s}$$
02

Calculate the rate of heat transfer

Now that we have the mass flow rate, we can calculate the rate of heat transfer using the specific heat capacity (\(c_p\)) and the temperature change. The temperature change is such that the rods enter at 30 °C and leave at 700 °C, so the overall change is $$(T_{out} - T_{in}) = 700 - 30 = 670\, °C$$ The rate of heat transfer (\(\dot{Q}\)) can be calculated using the following formula $$\dot{Q} = \dot{m} \times c_p \times \Delta T$$ Using the given values, $$\dot{Q} = 3.074 \times 0.465 \times 670 \approx 1007.98\, \mathrm{kJ/s} \approx 1008\, \mathrm{kJ/s}$$ So, the rate of heat transfer is 1008 kJ/s.
03

Calculate the rate of entropy generation

Finally, we'll calculate the rate of entropy generation. The entropy balance equation for an open system states: $$\frac{\Delta S_{gen}}{\Delta t} = \frac{\dot{Q}}{T_b}$$ where \(\Delta S_{gen}\) is the entropy generated, \(\Delta t\) is the time and \(T_b\) is the boundary temperature in Kelvin (oven temperature). First, we need to convert the given oven temperature in °C to Kelvin: $$T_b = 900 + 273.15 \approx 1173.15 K$$ Now, we can calculate the rate of entropy generation $$\frac{\Delta S_{gen}}{\Delta t} = \frac{1008 \times 10^3 \, \mathrm{J/s}}{1173.15 \, \mathrm{K}} \approx 859.79\, \mathrm{J/(s \cdot K)}$$ The rate of entropy generation is approximately 859.79 J/(s∙K). To summarize, (a) the rate of heat transfer to the rods in the oven is 1008 kJ/s, and (b) the rate of entropy generation associated with this heat transfer process is approximately 859.79 J/(s∙K).

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Most popular questions from this chapter

The compressed-air requirements of a plant at sea level are being met by a 90 -hp compressor that takes in air at the local atmospheric pressure of \(101.3 \mathrm{kPa}\) and the average temperature of \(15^{\circ} \mathrm{C}\) and compresses it to \(1100 \mathrm{kPa}\). An investigation of the compressed-air system and the equipment using the compressed air reveals that compressing the air to \(750 \mathrm{kPa}\) is sufficient for this plant. The compressor operates \(3500 \mathrm{h} / \mathrm{yr}\) at 75 percent of the rated load and is driven by an electric motor that has an efficiency of 94 percent. Taking the price of electricity to be \(\$ 0.105 / \mathrm{kWh},\) determine the amount of energy and money saved as a result of reducing the pressure of the compressed air.

A \(5-\mathrm{ft}^{3}\) rigid tank initially contains refrigerant- \(134 \mathrm{a}\) at 60 psia and 100 percent quality. The tank is connected by a valve to a supply line that carries refrigerant- 134 a at 140 psia and \(80^{\circ} \mathrm{F}\). The valve is now opened, allowing the refrigerant to enter the tank, and is closed when it is observed that the \(\operatorname{tank}\) contains only saturated liquid at 100 psia. Determine (a) the mass of the refrigerant that entered the tank, ( \(b\) ) the amount of heat transfer with the surroundings at \(70^{\circ} \mathrm{F}\), and \((c)\) the entropy generated during this process.

A piston-cylinder device contains steam that undergoes a reversible thermodynamic cycle. Initially the steam is at \(400 \mathrm{kPa}\) and \(350^{\circ} \mathrm{C}\) with a volume of \(0.3 \mathrm{m}^{3} .\) The steam is first expanded isothermally to \(150 \mathrm{kPa}\), then compressed adiabatically to the initial pressure, and finally compressed at the constant pressure to the initial state. Determine the net work and heat transfer for the cycle after you calculate the work and heat interaction for each process.

An adiabatic heat exchanger is to cool ethylene glycol \(\left(c_{p}=2.56 \mathrm{kJ} / \mathrm{kg} \cdot^{\circ} \mathrm{C}\right)\) flowing at a rate of \(2 \mathrm{kg} / \mathrm{s}\) from 80 to \(40^{\circ} \mathrm{C}\) by water \(\left(c_{p}=4.18 \mathrm{kJ} / \mathrm{kg} \cdot^{\circ} \mathrm{C}\right)\) that enters at \(20^{\circ} \mathrm{C}\) and leaves at \(55^{\circ} \mathrm{C}\). Determine \((a)\) the rate of heat transfer and \((b)\) the rate of entropy generation in the heat exchanger.

For an ideal gas with constant specific heats show that the compressor and turbine isentropic efficiencies may be written as $$\eta_{C}=\frac{\left(P_{2} / P_{1}\right)^{(k-1) / k}}{\left(T_{2} / T_{1}\right)-1} \text { and } \eta_{T}=\frac{\left(T_{4} / T_{3}\right)-1}{\left(P_{4} / P_{3}\right)^{(k-1) / k}-1}$$ The states 1 and 2 represent the compressor inlet and exit states and the states 3 and 4 represent the turbine inlet and exit states.

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