FUND OF ENG THERMODYN(LLF)+WILEYPLUS
9th Edition
ISBN: 9781119391777
Author: MORAN
Publisher: WILEY
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1 m3 of air is heated reversibly at constant pressure from 15°C to 350°C, and is then
cooled reversibly at constant volume back to the initial temperature. The initial
pressure is 1.03 bar. Take Cp, Çx and R as 1.005 kJ/kg,K , 0.718 kJ/kg. K and 0.287 kJ/kg,K
respectively.
1.
a) Sketch the processes on a T-s diagram.
b) Calculate
(i) the net heat flow, and
(ii) the overall change of entropy.
2. The work required to compress a gas reversibly according to pV130 = C is 67,790 J, if there is no
flow. Determine AU (in kJ) and Q (in kJ) if the gas is methane. For methane, k = 1.321, R = 518.45
J/kg-K, cv = 1.6187, cp = 2.1377 J/kg-K
please draw the P-V and
T-S diagrams
One-quarter lbmol of oxygen gas (O2) undergoes a process from p1 = 20 lbf/in2, T1 = 500oR to p2 = 150 lbf/in2. For the process W = -500 Btu and Q = -140.0 Btu. Assume the oxygen behaves as an ideal gas. Determine T2, in oR, and the change in entropy, in Btu/oR.
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- Three-tenths kmol of carbon monoxide (CO) in a piston- cylinder assembly undergoes a process from p1 = 150 kPa, T1 = 300 K to p2 = 500 kPa, T2 = 370 K. For the process, W = -300 kJ. Employing the ideal gas model, determine: (a) the heat transfer, in kJ. (b) the change in entropy, in kJ/K. Part A Employing the ideal gas model, determine the heat transfer, in kJ. kJ Save for Later Attempts: 0 of 1 used Submit Answer Part B The parts of this question must be completed in order. This part will be available when you complete the part above.arrow_forward1- 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_forwardOne-quarter Ibmol of oxygen gas (O₂) undergoes a process from p₁ = 20 lbf/in², T₁ = 500°R to p₂ = 150 lb/in². For the process W = -500 Btu and Q = -202.5 Btu. Assume the oxygen behaves as an ideal gas. Determine T2, in °R, and the change in entropy, in Btu/°R.arrow_forward
- Air contained in a rigid, insulated tank fitted with a paddle wheel, initially at 4 bar, 40 °C, and a volume of 0.2 m, is stirred until its temperature is 353 °C. Assuming the ideal gas model with k = 1.4 for the air, determine (a) the final pressure, in bar (b) the work, in kJ (c) the amount of entropy produced, in kJ/K. Ignore kinetic and potential energy.arrow_forwardEvaluate the work and heat transfer, each in kJ per kg refrigerantarrow_forwardQUESTION 19 The mass of CO2 is 0.066 kg in a system (with molar mass 44 kg/kmol), occupying a volume of 0.026 m³ at 0.9 bar is compressed reversibly until the pressure is 5.33 bar. If the molar (universal) gas constant as 8.3145 kJ/kmol K, calculate the final temperature (in C) when the process is isothermal. Answer to 3 d.p. No need for unitarrow_forward
- One-quarter lbmol of oxygen gas (O2) undergoes a process from p1 = 20 lbf/in2, T1 = 500oR to p2 = 150 lbf/in2. For the process W = -500 Btu and Q = -202.5 Btu. Assume the oxygen behaves as an ideal gas. Determine T2, in oR, and the change in entropy, in Btu/oR.arrow_forwardA rigid, well-insulated tank contains air. A partition in the tank separates 12 ft^3 of air at 14.7 lbf/in2, 40◦F (left side of the tank) from 10 ft^3 of air at 50 lbf/in2, 200◦F(right side of the tank), as illustrated in the figure. The partition is removed and air from the two sides mix until a final equilibrium state is attained. The air can be modeled as an ideal gas, and kinetic and potential energy effects can be neglected. (Note: values for the left side of the tank are denoted with a subscript L, and values for the right side of the tank are denoted with a subscript R). a) Determine the final temperature (in F) b) Determine the final pressure (in lbf/in^2) c) Calculate the amount of entropy produced, in Btu/R d) Is this mixing process reversible or irreversible?arrow_forwardThermodynamics, please help and show all work please.arrow_forward
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