Chapter 8: Problem 9
Does a refrigerator that has a higher COP necessarily have a higher second-law efficiency than one with a lower COP? Explain.
Chapter 8: Problem 9
Does a refrigerator that has a higher COP necessarily have a higher second-law efficiency than one with a lower COP? Explain.
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Get started for free\Air enters a compressor at ambient conditions of 15 psia and \(60^{\circ} \mathrm{F}\) with a low velocity and exits at 150 psia, \(620^{\circ} \mathrm{F},\) and \(350 \mathrm{ft} / \mathrm{s}\). The compressor is cooled by the ambient air at \(60^{\circ} \mathrm{F}\) at a rate of \(1500 \mathrm{Btu} / \mathrm{min} .\) The power input to the compressor is 400 hp. Determine \((a)\) the mass flow rate of air and \((b)\) the portion of the power input that is used just to overcome the irreversibilities.
Refrigerant-134a enters an adiabatic compressor at \(-30^{\circ} \mathrm{C}\) as a saturated vapor at a rate of \(0.45 \mathrm{m}^{3} / \mathrm{min}\) and leaves at \(900 \mathrm{kPa}\) and \(55^{\circ} \mathrm{C}\). Determine \((a)\) the power input to the compressor, \((b)\) the isentropic efficiency of the compressor, and \((c)\) the rate of exergy destruction and the second-law efficiency of the compressor. Take \(T_{0}=\) \(27^{\circ} \mathrm{C} .\) Answers: (a) \(1.92 \mathrm{kW},\) (b) 85.3 percent, \((c) 0.261 \mathrm{kW}\)
A crater lake has a base area of \(20,000 \mathrm{m}^{2},\) and the water it contains is \(12 \mathrm{m}\) deep. The ground surrounding the crater is nearly flat and is \(140 \mathrm{m}\) below the base of the lake. Determine the maximum amount of electrical work, in \(\mathrm{kWh}\) that can be generated by feeding this water to a hydroelectric power plant. Answer: \(95,500 \mathrm{kWh}\).
Argon gas enters an adiabatic compressor at \(120 \mathrm{kPa}\) and \(30^{\circ} \mathrm{C}\) with a velocity of \(20 \mathrm{m} / \mathrm{s}\) and exits at \(1.2 \mathrm{MPa}\) \(530^{\circ} \mathrm{C},\) and \(80 \mathrm{m} / \mathrm{s}\). The inlet area of the compressor is \(130 \mathrm{cm}^{2} .\) Assuming the surroundings to be at \(25^{\circ} \mathrm{C}\), determine the reversible power input and exergy destroyed.
In large steam power plants, the feedwater is frequently heated in closed feedwater heaters, which are basically heat exchangers, by steam extracted from the turbine at some stage. Steam enters the feedwater heater at \(1.6 \mathrm{MPa}\) and \(250^{\circ} \mathrm{C}\) and leaves as saturated liquid at the same pressure. Feedwater enters the heater at \(4 \mathrm{MPa}\) and \(30^{\circ} \mathrm{C}\) and leaves \(10^{\circ} \mathrm{C}\) below the exit temperature of the steam. Neglecting any heat losses from the outer surfaces of the heater, determine (a) the ratio of the mass flow rates of the extracted steam and the feedwater heater and \((b)\) the reversible work for this process per unit mass of the feedwater. Assume the surroundings to be at \(25^{\circ} \mathrm{C}\).
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