FUND OF ENG THERMODYN(LLF)+WILEYPLUS
9th Edition
ISBN: 9781119391777
Author: MORAN
Publisher: WILEY
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Steam undergoes an adiabatic expansion in a piston-cylinder assembly from 30 bar, 360°C to 3 bar, 240° C.
What is work in kJ per kg of steam for the process?
Calculate the amount of entropy produced, in kJ/K per kg of steam.
What is the maximum theoretical work that could be obtained from the given initial state to the same final pressure?
Steam undergoes an adiabatic expansion in a piston-cylinder assembly from 100 bar, 600°C to 1 bar, 160°C. What is work in kJ per kg
of steam for the process? Calculate the amount of entropy produced, in kJ/K per kg of steam. What is the magnitude of the maximum
theoretical work that could be obtained from the given initial state to the same final pressure?
Part A
What is work in kJ per kg of steam for the process?
W/m =
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- Using the rogers and Mayhew's table can you solve this as I'm struggling.arrow_forwardCarbon dioxide (molar mass 44 kg/kmol) expands rever sibly in a perfectly thermally insulated cylinder from 3.7 bar, 220 °C to a volume of 0.085 m'. If the initial volume occupied was 0.02 m', calculate the gas constant, adiabatic index, final pressure and work input. Assume nitrogen to be a perfect gas and take cv = 0.63 k J /kg K. Assessor's Signature Moderator's Signaturearrow_forward4.13 0.06 m' of ethane (molar mass 30 kg/kmol), at 6.9 bar and 260°C, is allowed to expand isentropically in a cylinder behind a piston to a pressure of 1.05 bar and a temperature of 107°C. Calculate 7, R, c,, c,. for ethane, and calculate the work donc during the expansion. Assume ethane to be a perfect gas. The same mass of ethane at 1.05 bar, 107°C, is compressed to 6.9 bar according to a law pr1. = constant. Calculate the final temperature of the ethane and the heat flow to or from the cylinder walls during the compression. Calculate also the change of entropy during the compression, and sketch both processes on a p-r and a T-s diagram. (1.219; 0.277 kJ/kg K; 1.542 kJ/kg K; 1.265 kJ/kg K; 54.2 kJ; 377.7°C; 43.4 kJ; 0.0862 kJ/K)arrow_forward
- 1- Steam initially at (15 bar, 300 C) expands reversibly and adiabatically in a steam turbine to (40 C°). Determine the ideal work output of the turbine per kg of steam and find the dryness fraction at the turbine exit. [Ans. 90 kj/kg, 0.825]arrow_forwardCarbon dioxide (molar mass 44 kg/kmol) expands reversibly in a perfectly thermally insulated cylinder from 3.7 bar, 220 0C to a volume of 0.085 m3. If the initial volume occupied was 0.02 m3, calculate the gas constant, adiabatic index, final pressure and work input. Assume nitrogen to be a perfect gas and take cv = 0.63 k J / k g K.arrow_forwardOne-quarter Ibmol of oxygen gas (O2) undergoes a process from p1 = 20 Ib/in?, T1 = 500°R to p2 = 150 lb;/in?. For the process W = -500 Btu and Q = -127.5 Btu. Assume the oxygen behaves as an ideal gas. Determine T2, in °R, and the change in entropy, in Btu/°R. Step 1 Determine T2, in °R. T2 = °R Save for Later Attempts: 0 of 1 used Submit Answer Step 2 The parts of this question must be completed in order. This part will be available when you complete the part above.arrow_forward
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