Fundamentals Of Engineering Thermodynamics
9th Edition
ISBN: 9781119391388
Author: MORAN, Michael J., SHAPIRO, Howard N., Boettner, Daisie D., Bailey, Margaret B.
Publisher: Wiley,
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Determine the specific exergy of saturated water vapor at 137 °C, where To = 313K, Po = 101.3kPa. Assume the velocity and
elevation is zero with reference to the environment.
You must use following tables to solve this problem. (answer to 2 decimal)
Saturated water temperature table
Sat Liq.
Temp.,
Sat Liq. Sat Liq.
Sat Liq.
vf
uf
hf
sf
°C
m3/kg
kJ/kg
kJ/kg
kJ/kg.K
30
0.001004
125.73
125.74
0.4368
35
0.001006
146.63
146.64
0.5051
40
0.001008
167.53
167.53
0.5724
45
0.00101
188.43
188.44
0.6386
Saturated water temperature table
Temp.,
Sat. Vap.
Sat. Vap.
Sat. Vap.
Sat. Vap.
hg
kJ/kg
vg
ug
sg
°C
m3/kg
kJ/kg
kJ/kg.K
125
0.7508
2534.5
2713.5
7.0745
126
0.7358
2535.5
2714.8
7.0649
127
0.7208
2536.5
2716.1
7.0553
128
0.7058
2537.5
2717.4
7.0457
129
0.6908
2538.5
2718.7
7.0361
130
0.6758
2539.5
2720.0
7.0265
131
0.6608
2540.5
2721.4
7.0169
132
0.6458
2541.4
2722.7
7.0073
133
0.6308
2542.4
2724.0
6.9977
134
0.6158
2543.4
2725.3
6.9881
6.9785
135
0.6008
2544.4
2726.6
136
0.5858
2545.4
2727.9…
A balloon filled with helium at 20°C, 1 bar and a volume of 0.5 m³ is moving with a velocity of 15 m/s at an
elevation of 0.5 km relative to an exergy reference environment for which To = 20°C, po = 1 bar. Using the
ideal gas model with k = 1.67, determine the specific exergy of the helium, in kJ.
Answer please
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Similar questions
- At a pressure of 1 bar, a temperature of 17 °C and a mass flow of 0.3 kg/s, air enters a stable insulated compressor and exits at 3 bar, 147 °C. Determine the power required by the compressor and the exergy destruction in kW. Express the exergy disappearance as a percentage according to the power required by the compressor. Changes in kinetic and potential energy will be neglected. dead state; T0=17 °C, P0=1 bararrow_forwardCorrect answer will be upvoted.THANK YOU!!!arrow_forward3.1 For discussion: (a) Is it possible for exergy to be negative? Discuss. (b) Consider an evacuated space with volume V as the system. Eval- uate its exergy and discuss. PH associated with (c) Is it possible for the specific physical exergy e' a stream of matter to be negative? Discuss.arrow_forward
- Apply exergy balance to closed systems and control volumes.arrow_forwardFour kilograms of a two-phase liquid-vapor mixture of water initially at 300°C and x, = 0.5 undergo the two different processes 7.33 described below. In each case, the mixture is brought from the initial state to a saturated vapor state, while the volume remains constant. For each process, determine the change in exergy of the water, the net amounts of exergy transfer by work and heat, and the amount of exergy destruction, each in kJ. Let To = 300 K, Po =1 bar, and ignore the effects of motion and gravity. Comment on the difference between the exergy destruction values. a. The process is brought about adiabatically by stirring the mixture with a paddle wheel. Answer b. The process is brought about by heat transfer from a thermal reservoir at 610 K. The temperature of the water at the location where the heat transfer occurs is 610 K Answerarrow_forwardIf heating from saturated liquid to saturated vapor would occur at 100°C (373.15 K), evaluate the exergy transfers accompanying heat transfer and work, each in kJ/kg. Ans. 484, 0.arrow_forward
- EXERGY TRANSFER BY HEAT, WORK, AND MASSarrow_forwardPossible solution as soon as possiblearrow_forwardDetermine the change in exergy in kJ for each of the following processes in the system with 1 kg of steam at 20 bar and 240 °C initially. a) In case the system is heated to double its volume at constant pressure. b) In case of expansion by doubling the system volume isothermally. dead state; T0=20 °C, P0=1 bararrow_forward
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