Chapter 8: Problem 59
Steam is throttled from 7 MPa and \(500^{\circ} \mathrm{C}\) to a pressure of 1 MPa. Determine the decrease in exergy of the steam during this process. Assume the surroundings to be at \(25^{\circ} \mathrm{C} .\)
Chapter 8: Problem 59
Steam is throttled from 7 MPa and \(500^{\circ} \mathrm{C}\) to a pressure of 1 MPa. Determine the decrease in exergy of the steam during this process. Assume the surroundings to be at \(25^{\circ} \mathrm{C} .\)
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An insulated piston-cylinder device contains 0.8 L of saturated liquid water at a constant pressure of 120 kPa. An electric resistance heater inside the cylinder is turned on, and electrical work is done on the water in the amount of 1400 kJ. Assuming the surroundings to be at \(25^{\circ} \mathrm{C}\) and \(100 \mathrm{kPa}\), determine \((a)\) the minimum work with which this process could be accomplished and ( \(b\) ) the exergy destroyed during this process.
Refrigerant- 134 a is converted from a saturated liquid to a saturated vapor in a closed system using a reversible constant pressure process by transferring heat from a heat reservoir at \(6^{\circ} \mathrm{C}\). From second-law point of view, is it more effective to do this phase change at \(100 \mathrm{kPa}\) or \(180 \mathrm{kPa} ?\) Take \(T_{0}=25^{\circ} \mathrm{C}\) and \(P_{0}=100 \mathrm{kPa}\).
Combustion gases enter a gas turbine at \(900^{\circ} \mathrm{C}\) \(800 \mathrm{kPa},\) and \(100 \mathrm{m} / \mathrm{s}\) and leave at \(650^{\circ} \mathrm{C}, 400 \mathrm{kPa},\) and \(220 \mathrm{m} / \mathrm{s} .\) Taking \(c_{p}=1.15 \mathrm{kJ} / \mathrm{kg} \cdot^{\circ} \mathrm{C}\) and \(k=1.3\) for the combustion gases, determine \((a)\) the exergy of the combustion gases at the turbine inlet and ( \(b\) ) the work output of the turbine under reversible conditions. Assume the surroundings to be at \(25^{\circ} \mathrm{C}\) and \(100 \mathrm{kPa}\). Can this turbine be adiabatic?
Cold water \(\left(c_{p}=4.18 \mathrm{kJ} / \mathrm{kg} \cdot^{\circ} \mathrm{C}\right)\) leading to a shower enters a well-insulated, thin-walled, double-pipe, counterflow heat exchanger at \(15^{\circ} \mathrm{C}\) at a rate of \(0.25 \mathrm{kg} / \mathrm{s}\) and is heated to \(45^{\circ} \mathrm{C}\) by hot water \(\left(c_{p}=4.19 \mathrm{kJ} / \mathrm{kg} \cdot^{\circ} \mathrm{C}\right)\) that enters at \(100^{\circ} \mathrm{C}\) at a rate of \(3 \mathrm{kg} / \mathrm{s}\). Determine \((a)\) the rate of heat transfer and \((b)\) the rate of exergy destruction in the heat exchanger. Take \(T_{0}=25^{\circ} \mathrm{C}\)
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