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Mechanical Engineering

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Apr 3, 2024

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Chapter 6 homework 6.6 Using the appropriate table, determine the indicated property for a process in which there is no change in specific entropy between state 1 and state 2. a. water, p 1 = 14.7 lbf/in 2 , T 1 = 500°F, p 2 = 100 lbf/ in 2 . Find T 2 in °F. 1017 b. water, T 1 = 10°C, x 1 = 0.75, saturated vapor at state 2. Find p 2 in bar. 6.897 c. air as an ideal gas, T 1 = 27°C, p 1 = 1.5 bar, T 2 = 127°C. Find p 2 in bar. 4.119 d. air as an ideal gas, T 1 = 100°F, p 1 = 3 atm, p 2 = 2 atm. Find T 2 in °F. 38.7 e. Refrigerant 134a, T 1 = 20°C, p 1 = 5 bar, p 2 = 1 bar. Find v 2 in m 3 /kg. 0.188 6.7 Air in a piston cylinder assembly undergoes a process from state 1, where T 1 = 300 K, p 1 = 100 kPa, to state 2, where T 2 = 500 K, p 2 = 650 kPa. Using the ideal gas model for air, determine the change in specific entropy between these states, in kJ/kg · K, if the process occurs (a) without internal irreversibilities, (b) with internal irreversibilities. −0.0197 6.25 Three m 3 of air in a rigid, insulated container fitted with a paddle wheel is initially at 295 K, 200 kPa. The air receives 1546 kJ of work from the paddle wheel. Assuming the ideal gas model, determine for the air (a) the mass, in kg, (b) final temperature, in K, and (c) the amount of entropy produced, in kJ/K. 7.087, 592.6, 0.5106 kJ/kg/K or 3.6135 kJ/K error in book solution, and I also made an error fixed now. 6.56 Air enters a compressor operating at steady state at 15 lbf/in 2 , 80°F and exits at 400°F. Stray heat transfer and kinetic and potential energy effects are negligible. Assuming the ideal gas model for the air, determine the maximum theoretical pressure at the exit, in lbf/in 2 . 77.35 6.61 An open feedwater heater is a direct-contact heat exchanger used in vapor power plants. Shown in Fig. P6.61 are operating data for an open feedwater heater with H 2 O as the working fluid operating at steady state. Ignoring stray heat transfer from the outside of the heat exchanger to its surroundings and kinetic and potential energy effects, determine the rate of entropy production, in kW/K. 9.51 (66.32, 13.68)
6.80 Air in a piston cylinder assembly expands isentropically from T 1 = 1800°R, p 1 = 2000 lbf/in 2 , to p 2 = 20 lbf/in 2 . Assuming the ideal gas model, determine the temperature at state 2, in °R, using (a) data from Table A-22E, and (b) a constant specific heat ratio, k = 1.4. Compare the values obtained in parts (a) and (b) and comment. 510.4, 482.9 6.81 Air in a piston-cylinder assembly is compressed isentropically from state 1, where T 1 = 35°C, to state 2, where the specific volume is one-tenth of the specific volume at state 1. Applying the ideal gas model and assuming variations in specific heat, determine (a) T 2 , in °C, and (b) the work, in kJ/kg. 474.5, 330.2 6.85 Air within a piston cylinder assembly, initially at 30 lbf/in 2 , 510°R, and a volume of 6 ft 3 , is compressed isentropically to a final volume of 1.2 ft 3 . Assuming the ideal gas model with k = 1.4 for the air, determine the (a) mass, in lb, (b) final pressure, in lbf/in 2 , (c) final temperature, in °R, and (d) work, in Btu. 0.953, 285.55, 970.9, -75.3 6.88 The accompanying table provides steady-state data for an isentropic expansion of steam through a turbine. For a mass flow rate of 2.55 kg/s, determine the power developed by the turbine, in MW. Ignore the effects of potential energy. 1.0
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