The basic cycle for a steam power plant is shown in Figure 1. The turbine operates adiabatically with inlet steam at 80 bar and 600°C, and the exhaust steam enters the condenser at 50°C with a quality of 0.96. Saturated liquid water leaves the condenser and is pumped to the boiler. Neglecting pump work and kinetic- and

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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H3 - H2
Efficiency of turbine
H- H2
H = (1– x')Hug +x'Hvap
S2 = (1 – x')Suq + x'Syap
%D
H2 – H3
Efficiency of cycle =
H2 – H1
SATURATED STEAM TEMPERATURE TABLE
Int. Ener.
kJ/kg
Sat.
Spec. vol.
m2=kg
Sat.
liq.
Vr
X1000
1.0002
Enthalpy
kJ/kg
Sat.
Entropy
kJ=(kg°K)
Sat.
Sat.
liq.
Sat.
Sat.
Sat.
vap.
Vg
liq.
Uf
vap.
Ug
liq.
he
vap.
hg
vap.
Sg
°C
bar
Sf
0.01
0.01
2501
2509
2511
2512
2516
2520
2522
2523
2525
0.0061
0.0081
0.0087
0.0093
0.0107
0.0123
0.0131
0.0140
0.0150
0.0160
0.0170
0.0182
0.0194
0.0206
0.0220
0.0234
0.0249
0.0264
0.0281
0.0298
0.0317
0.0336
0.0357
0.0378
0.0401
0.0425
206.1
0.01
2376
9.156
1.0001
1.0001
1.0001
1.0001
1.0001
4.
157.2
16.79
21.00
25.21
33.61
42.01
46.19
50.40
54.59
58.80
2381
2383
2384
2387
2389
2391
2392
2393
2394
16.79
21
25.21
33.61
42.01
46.19
50.4
54.59
58.8
62.99
67.17
71.36
75.57
79.76
83.94
88.13
0.061
0.0762
0.0912
0.1212
0.151
0.1658
0.1806
0.1953
0.2099
0.2245
0.239
2535
0.2679
9.051
9.026
9.000
8.950
8.901
8.876
8.852
8.828
147.1
10
11
12
13
137.7
120.9
106.4
99.86
93.79
88.13
82.85
1.0007
1.0007
1.0007
1.0007
14
2527
77.93
73.34
69.05
65.04
61.30
57.79
54.52
51.45
48.58
45.89
8.805
8.781
8.758
8.735
8.712
8.690
8.667
8.645
8.623
8.601
8.579
8.558
8.537
8.515
15
16
17
18
19
20
21
22
23
24
25
26
27
1.0007
1.0013
1.0013
1.0013
1.0013
1.002
1.002
1.002
1.0026
1.0026
1.0032
1.0032
1.0032
62.99
67.17
71.36
75.57
79.76
83.94
88.13
2396
2397
2399
2400
2401
2403
2404
2406
2407
2409
2410
2411
2412
2414
2415
2416
2529
2531
2533
2534
2536
2538
2540
2542
2544
0.2823
0.2966
0.3108
0.3251
0.3392
92.32
96.50
100.7
104.9
109.0
113.2
117.4
121.6
125.8
92.32
96.5
100.7
104.9
109.0
113.2
0.3533
0.3673
0.3814
0.3953
0.4093
0.4231
0.4369
2545
43.36
41.00
38.78
2547
2549
2551
28
1.0038
1.0038
36.69
34.73
32.90
117.4
121.6
125.8
2553
2554
2556
8.495
8.474
8.453
29
30
1.0045
Transcribed Image Text:H3 - H2 Efficiency of turbine H- H2 H = (1– x')Hug +x'Hvap S2 = (1 – x')Suq + x'Syap %D H2 – H3 Efficiency of cycle = H2 – H1 SATURATED STEAM TEMPERATURE TABLE Int. Ener. kJ/kg Sat. Spec. vol. m2=kg Sat. liq. Vr X1000 1.0002 Enthalpy kJ/kg Sat. Entropy kJ=(kg°K) Sat. Sat. liq. Sat. Sat. Sat. vap. Vg liq. Uf vap. Ug liq. he vap. hg vap. Sg °C bar Sf 0.01 0.01 2501 2509 2511 2512 2516 2520 2522 2523 2525 0.0061 0.0081 0.0087 0.0093 0.0107 0.0123 0.0131 0.0140 0.0150 0.0160 0.0170 0.0182 0.0194 0.0206 0.0220 0.0234 0.0249 0.0264 0.0281 0.0298 0.0317 0.0336 0.0357 0.0378 0.0401 0.0425 206.1 0.01 2376 9.156 1.0001 1.0001 1.0001 1.0001 1.0001 4. 157.2 16.79 21.00 25.21 33.61 42.01 46.19 50.40 54.59 58.80 2381 2383 2384 2387 2389 2391 2392 2393 2394 16.79 21 25.21 33.61 42.01 46.19 50.4 54.59 58.8 62.99 67.17 71.36 75.57 79.76 83.94 88.13 0.061 0.0762 0.0912 0.1212 0.151 0.1658 0.1806 0.1953 0.2099 0.2245 0.239 2535 0.2679 9.051 9.026 9.000 8.950 8.901 8.876 8.852 8.828 147.1 10 11 12 13 137.7 120.9 106.4 99.86 93.79 88.13 82.85 1.0007 1.0007 1.0007 1.0007 14 2527 77.93 73.34 69.05 65.04 61.30 57.79 54.52 51.45 48.58 45.89 8.805 8.781 8.758 8.735 8.712 8.690 8.667 8.645 8.623 8.601 8.579 8.558 8.537 8.515 15 16 17 18 19 20 21 22 23 24 25 26 27 1.0007 1.0013 1.0013 1.0013 1.0013 1.002 1.002 1.002 1.0026 1.0026 1.0032 1.0032 1.0032 62.99 67.17 71.36 75.57 79.76 83.94 88.13 2396 2397 2399 2400 2401 2403 2404 2406 2407 2409 2410 2411 2412 2414 2415 2416 2529 2531 2533 2534 2536 2538 2540 2542 2544 0.2823 0.2966 0.3108 0.3251 0.3392 92.32 96.50 100.7 104.9 109.0 113.2 117.4 121.6 125.8 92.32 96.5 100.7 104.9 109.0 113.2 0.3533 0.3673 0.3814 0.3953 0.4093 0.4231 0.4369 2545 43.36 41.00 38.78 2547 2549 2551 28 1.0038 1.0038 36.69 34.73 32.90 117.4 121.6 125.8 2553 2554 2556 8.495 8.474 8.453 29 30 1.0045
The basic cycle for a steam power plant is shown in Figure 1. The turbine operates
adiabatically with inlet steam at 80 bar and 600°C, and the exhaust steam enters the
condenser at 50°C with a quality of 0.96. Saturated liquid water leaves the
condenser and is pumped to the boiler. Neglecting pump work and kinetic- and
potential-energy changes determine
Thermal efficiency of the cycle .1
Turbine efficiency .2
2
Boiler
w, (turbine)
Turbine
w, (pump)
Condenser
Transcribed Image Text:The basic cycle for a steam power plant is shown in Figure 1. The turbine operates adiabatically with inlet steam at 80 bar and 600°C, and the exhaust steam enters the condenser at 50°C with a quality of 0.96. Saturated liquid water leaves the condenser and is pumped to the boiler. Neglecting pump work and kinetic- and potential-energy changes determine Thermal efficiency of the cycle .1 Turbine efficiency .2 2 Boiler w, (turbine) Turbine w, (pump) Condenser
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