FUND OF ENG THERMODYN(LLF)+WILEYPLUS
9th Edition
ISBN: 9781119391777
Author: MORAN
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…
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- Exergy of a Flow Stream: Flow (or Stream) Exergy.arrow_forwardThermodynamics. 1) For a closed system, as the exergy reference environment temperature ___________, the exergy destruction rate decreases 2) Which of the following statements does not describe the exergy reference environment? It is large in extent. It has a uniform temperature. It is incompressible. It has a uniform pressure. 3) Air within a piston–cylinder assembly undergoes an expansion process from an initial volume of 0.5 m3 to 1 m3. The dead state pressure is 100 kPa. If the work associated with the process is 60 kJ, determine the exergy transfer accompanying work, in kJ.arrow_forwardFAST ANSWERS WILL BE GIVEN UPVOTE.arrow_forward
- Answer pleasearrow_forwardProblems 1-8 are a continuation of HW #6. All answers should have 4 or 5 significant figures. For problems 1-8 please solve for u (specific internal.energy) and h (specific enthalpy), for water (H2O), given the following information. 1. H2O, T = 150°C, P = 50 bar 2. H2O, T = 200°C, P = 10 bar 3. H20, T = 120°C, v = 0.5000 m3/kg 4. H20, P = 5 bar, u = 0.7000 m/kgarrow_forward7.36 At steady state, hot gaseous products of combustion from a gas turbine cool from 3000°F to 250°F as they flow through a pipe. Owing to negligible fluid friction, the flow occurs at nearly constant pressure. Applying the ideal gas model with ₂ = 0.3 Btu/lb/ºR, determine the exergy transfer accompanying heat transfer from the gas, in Btu per lb of gas flowing. Let T. = 80°F and ignore the effects of motion and gravity. -568.43arrow_forward
- a) Using the second law of thermodynamics, describe exergy d law of thermodynamics, describe exergy. Explain the different types of exergy b) What do you understand by the term reference environme c) Determine the specific exergy of saturated water vapour we having a velocity of 30m/s and an elevation of 6m, each relative to an exergy reference environment where T = 298K. P. = 1 atm and g = 9.8m/s. d) Steam enters a turbine with a pressure of 30 bar, a temperature of 400°C, a velocity of 160 m/s and exits as saturated vapor at 100°C with a velocity of 100 m/s. At steady state, the turbine develops work at a rate of 540 kJ per kg of steam flowing through the turbine. The heat transfer rate (cv/m = -22.6 – Heat transfer between the turbine and its surroundings occurs at an average outer surface temperature of 350 K. Neglect the change in potential energy between the inlet and exit of the turbine, and assume that To = 25°C. Po =1 atm. Using a neat sketch, determine: i net exergy carried…arrow_forwardEXERGY TRANSFER BY HEAT, WORK, AND MASSarrow_forwardi) Describe what is threshold problems? ii) Figure 1 illustrates a composite curve for a set of process stream data. With the aid of a diagram, explain what will happen to the utility consumptions if AT min is further reduced until AT min < AT threshold: 200 180 Qn 160 140 120 100 AT threshold 80 60 40 20 50 100 150 200 250 300 350 H (KW) Figure 1 TEMPERATURE (°C)arrow_forward
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