carefully and answer with complete solution and units. Use the steam tables provided and use 4 decimal places for solving. Final answer shown are in 2 decimal places. Draw the T-S diagrams properly with respect to the saturation line 1.) Consider a steam power plant operating on the ideal Rankine cycle. The boiler is maintained at 4
carefully and answer with complete solution and units. Use the steam tables provided and use 4 decimal places for solving. Final answer shown are in 2 decimal places. Draw the T-S diagrams properly with respect to the saturation line 1.) Consider a steam power plant operating on the ideal Rankine cycle. The boiler is maintained at 4
Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
ChapterMA: Math Assessment
Section: Chapter Questions
Problem 1.1MA
Related questions
Question
Read the questions carefully and answer with complete solution and units. Use the steam tables provided and use 4 decimal places for solving. Final answer shown are in 2 decimal places. Draw the T-S diagrams properly with respect to the saturation line
1.) Consider a steam power plant operating on the ideal Rankine cycle.
The boiler is maintained at 4 MPa, and the condenser at 10 kPa. The steam quality leaving the turbine is at 80%.
a.) Draw the proper T-S
diagram of the cycle with proper label for the points. b.) Find the temperature of the steam entering the turbine, Qa, Qr, Wt, Wp, Wnet,
efficiency, and steam rate.
![4.0 (250.40)
4.1 (251.87)
p(t Sat.)
10 v
10 v
49.78 2602.3 2801.4
6.0701
48.53 2601.9 2800.9
6.0597
Sat.
240
245
48.60 2585.9 2780.3
6.0297
47.04 2580.7 2773.6
6.0074
49.69 260LI 2799,9
30.74 2615.5 2818.5
51.74 2629.4 2836.3
52.71 2642.7 2853.5 6.1683
53.65 2655.5 2870.1 6.1990
6.0672
6.1026
6.1362
48.13 2596.3 2793.6
49.17 2611.T 2812.7
50.17 2625.2 2830.9
51.14 2638.8 2848.5
52.07 2651.9 2865.4 6.1805
6.0459
6.0822
6.1165
6.1493
250
255
260
265
270
54.57 2667.9 2886.2 6.2285
55.46 2680.0 2901.8 6.2568
56.33 2691.7 2917.0 6.2842
57.18 2703.2 2931.9 6.3108
58.02 2714.4 2946.4 6.3365
52.98 2664.5 2881.7
53.86 2676.7 2897.6
54.72 2688.7 2913.0
55.56 2700.3 2928.1
56.39 2711.6 2942.8
6.2105
6.2393
6.2671
6.2940
6.3200
275
280
285
290
295
58.84 2725.3 2960.7 6.3615
60.44 2746.7 2988.5 6.4095
61.99 2767.4 3015.4 6.4553
63.51 2787.6 3041.6 6.4991
64.99 2807.3 3067.3 6.5413
57.20 2722.7 2957.2
58.77 2744.3 2985.3
60.30 2765.2 3012.5
61.79 2785.6 3038.9
63.25 2805.4 3064.8 6.5268
6.3453
6.3939
6.4401
6.4843
300
310
320
330
340
64.68 2824.9 3090.1
66.08 2844.1 3115.0 6.6075
67.47 2863.0 3139.6 6.6460
68.83 2881.7 3163.9
70.18 2900.2 3188.0
6.5678
66.45 2826.7 3092.5 6.5821
67.88 2845.7 3117.2 6.6215
69.29 2864.6 3141.7 6.6598
70.68 2883.2 3165.9 6.6971
72.05 2901.6 3189.8
350
360
370
380
390
6.6834
6.7200
6.7335](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2Fc6dbb6f8-953d-4a43-b7a6-42f686a0b01b%2Fcc2d7b17-386f-4321-99a3-8d07ea8ddd08%2Fket7reb_processed.jpeg&w=3840&q=75)
Transcribed Image Text:4.0 (250.40)
4.1 (251.87)
p(t Sat.)
10 v
10 v
49.78 2602.3 2801.4
6.0701
48.53 2601.9 2800.9
6.0597
Sat.
240
245
48.60 2585.9 2780.3
6.0297
47.04 2580.7 2773.6
6.0074
49.69 260LI 2799,9
30.74 2615.5 2818.5
51.74 2629.4 2836.3
52.71 2642.7 2853.5 6.1683
53.65 2655.5 2870.1 6.1990
6.0672
6.1026
6.1362
48.13 2596.3 2793.6
49.17 2611.T 2812.7
50.17 2625.2 2830.9
51.14 2638.8 2848.5
52.07 2651.9 2865.4 6.1805
6.0459
6.0822
6.1165
6.1493
250
255
260
265
270
54.57 2667.9 2886.2 6.2285
55.46 2680.0 2901.8 6.2568
56.33 2691.7 2917.0 6.2842
57.18 2703.2 2931.9 6.3108
58.02 2714.4 2946.4 6.3365
52.98 2664.5 2881.7
53.86 2676.7 2897.6
54.72 2688.7 2913.0
55.56 2700.3 2928.1
56.39 2711.6 2942.8
6.2105
6.2393
6.2671
6.2940
6.3200
275
280
285
290
295
58.84 2725.3 2960.7 6.3615
60.44 2746.7 2988.5 6.4095
61.99 2767.4 3015.4 6.4553
63.51 2787.6 3041.6 6.4991
64.99 2807.3 3067.3 6.5413
57.20 2722.7 2957.2
58.77 2744.3 2985.3
60.30 2765.2 3012.5
61.79 2785.6 3038.9
63.25 2805.4 3064.8 6.5268
6.3453
6.3939
6.4401
6.4843
300
310
320
330
340
64.68 2824.9 3090.1
66.08 2844.1 3115.0 6.6075
67.47 2863.0 3139.6 6.6460
68.83 2881.7 3163.9
70.18 2900.2 3188.0
6.5678
66.45 2826.7 3092.5 6.5821
67.88 2845.7 3117.2 6.6215
69.29 2864.6 3141.7 6.6598
70.68 2883.2 3165.9 6.6971
72.05 2901.6 3189.8
350
360
370
380
390
6.6834
6.7200
6.7335
![Specific Volume
Li
10°, 10,
Internal Energy
Sal
Liquld
Tep
Enthalpy
Sat,
Entropy
MP
Sat.
Vapor
Sat.
Vapor
Sat,
Liquid
Sat.
Vapor
Evap.
Liquid
Evap.
Evap.
uy
h,
h,
006113
.0007
0008
.0009
01
1.89
3.77
5.45
1.0002 206 136
1.0001 181 255
1,0001 159 675
1.0001 142 789
.00 2.75.3 2375.3
7.90 2370.0 2377.9
15.81 2364.7 2380.6
22.88 2360.0 2382.9
.01 2501.3 2501.4
7.91 2496.9 2504.8
15.81 2492.5 2508.3
22.89 2488.5 2511.4
0000 9.1562 9.1562
.0288 9.0775 9.1064
.0575 8.9999 9.0573
0829 8.9312 9.0142
.0010
0011
.0012
.0013
.0014
6.98
8.37
9.66
10.86
11.98
1.0002 129 208
1.0002 118 042
1.0003 108 696
1.0004 100 755
1.0005
29.30 2355.7 2385.0
35.17 2351.8 2386.9
40.58 2348.1 2388.7
45.60 2344.7 2390.3
50.31 2341.6 2391.9
29.30 2484.9 2514.2
35.17 2481.6 2516.8
40.58 2478.6 2519.1
45.60 2475.7 2521.3
50.31 2473.1 2523.4
.1059 8.8697 8.9756
1268 8.8140 8.9408
.1460 8.7631! 8.9091
1637 8.7162 8.8799
.1802 8.6727 8.8529
93 922
.0015
.0016
.0017
0018
.0019
13.03
14.02
14.95
15.84
16.69
1.0007
1.0008
1.0009
1.0010
1.0012
87 980
82 763
78 146
14 030
70 337
54.71 2338.6 2393.3
58.87 2335.8 2394.7
62.80 2333.2 2396.0
66.53 2330.7. 2397.2
70.09 2328.3 2398.4
54.71 2470.6 2525.3
58.87 2468.3 2527.1
62.80 2466.0 2528.8
66.54 2463.9 2530.5
70.10 2461.9 2532.0
.1957 8.6322 8.8279
2102 8.5943 8.8044
2238 8.5586 8.7825
2368 8.5250 8.7618
2491 8.4931 8.7422
.0050
.0055
.0060
.0065
.0070
32.88
34.58
36.16
37.63
39.00
1.0053
1.0058
1.0064
1.0069
1.0074
28 192
25 769
23 739
22 014
20 530
137.81 2282.7 2420.5
144.94 2277.9 2422.8
151.53 2273.4 2425.0
157.66 2269.3 2426.9
163.39 2265.4 2428.8
137.82 2423.7 2561.5
144.95 2419.6 2564.5
151.53 2415.9 2567.4
157.67 2412.4 2570.0
163.40 2409.1 2572.5
4764 7.9187 8.3951
4997 7.8616 8.3613
5210 7.8094 8.3304
5408 7.7613 8.3020
5592 7.7167 8.2758
.0075
.0080
.0085
.0090
.0095
40.29
41.51
42.67
43.76
44.81
1.0079
1.0084
1.0089
1.0094
1.0098
19 238
18 103
17099
16 203
15 399
168.78 2261.7 2430.5
173.87 2258.3 2432.2
178.69 2255.0 2433.7
183.27 2251.9 2435.2
187.64 2248.9 2436.6
168.79 2406.0 2574.8
173.88 2403.1 2577.0
178.70 2400.3 2579.0
183.29 2397.7 2581.0
187.65 2395.2 2582.9
5764 7.6750 8.2515
5926 7.6361 8.2287
6079 7.5994 8.2073
6224 7.5648 8.1872
.6362 7.5321 8.1682
.010
.011
.012
.013
.014
45.81
47.69
49.42
51.04
52.55
1.0102
10111
1.0119
1.0126
1.0134
14 674
13 415
12 361
il 465
10 693
191.82 2246.1 2437.9
199.66 2240.8 2440.4
206.91 2235,8 2442.7
213.66 2231.2 2444.9
219.98 2226.9 2446.9
191.83 2392.8 2584.7
199.67 2388.3 2588.0
206.92 2384.1 2591.1
213.67 2380.2 2593.9
219.99 2376.6 2596.6
.6493 7.5009 8.1502
6738 7.4430 8.1168
.6963 7.3900 8.0863
.7172 7.3412 8.0584
.7366 7.2959 8.0325](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2Fc6dbb6f8-953d-4a43-b7a6-42f686a0b01b%2Fcc2d7b17-386f-4321-99a3-8d07ea8ddd08%2Fg82515_processed.jpeg&w=3840&q=75)
Transcribed Image Text:Specific Volume
Li
10°, 10,
Internal Energy
Sal
Liquld
Tep
Enthalpy
Sat,
Entropy
MP
Sat.
Vapor
Sat.
Vapor
Sat,
Liquid
Sat.
Vapor
Evap.
Liquid
Evap.
Evap.
uy
h,
h,
006113
.0007
0008
.0009
01
1.89
3.77
5.45
1.0002 206 136
1.0001 181 255
1,0001 159 675
1.0001 142 789
.00 2.75.3 2375.3
7.90 2370.0 2377.9
15.81 2364.7 2380.6
22.88 2360.0 2382.9
.01 2501.3 2501.4
7.91 2496.9 2504.8
15.81 2492.5 2508.3
22.89 2488.5 2511.4
0000 9.1562 9.1562
.0288 9.0775 9.1064
.0575 8.9999 9.0573
0829 8.9312 9.0142
.0010
0011
.0012
.0013
.0014
6.98
8.37
9.66
10.86
11.98
1.0002 129 208
1.0002 118 042
1.0003 108 696
1.0004 100 755
1.0005
29.30 2355.7 2385.0
35.17 2351.8 2386.9
40.58 2348.1 2388.7
45.60 2344.7 2390.3
50.31 2341.6 2391.9
29.30 2484.9 2514.2
35.17 2481.6 2516.8
40.58 2478.6 2519.1
45.60 2475.7 2521.3
50.31 2473.1 2523.4
.1059 8.8697 8.9756
1268 8.8140 8.9408
.1460 8.7631! 8.9091
1637 8.7162 8.8799
.1802 8.6727 8.8529
93 922
.0015
.0016
.0017
0018
.0019
13.03
14.02
14.95
15.84
16.69
1.0007
1.0008
1.0009
1.0010
1.0012
87 980
82 763
78 146
14 030
70 337
54.71 2338.6 2393.3
58.87 2335.8 2394.7
62.80 2333.2 2396.0
66.53 2330.7. 2397.2
70.09 2328.3 2398.4
54.71 2470.6 2525.3
58.87 2468.3 2527.1
62.80 2466.0 2528.8
66.54 2463.9 2530.5
70.10 2461.9 2532.0
.1957 8.6322 8.8279
2102 8.5943 8.8044
2238 8.5586 8.7825
2368 8.5250 8.7618
2491 8.4931 8.7422
.0050
.0055
.0060
.0065
.0070
32.88
34.58
36.16
37.63
39.00
1.0053
1.0058
1.0064
1.0069
1.0074
28 192
25 769
23 739
22 014
20 530
137.81 2282.7 2420.5
144.94 2277.9 2422.8
151.53 2273.4 2425.0
157.66 2269.3 2426.9
163.39 2265.4 2428.8
137.82 2423.7 2561.5
144.95 2419.6 2564.5
151.53 2415.9 2567.4
157.67 2412.4 2570.0
163.40 2409.1 2572.5
4764 7.9187 8.3951
4997 7.8616 8.3613
5210 7.8094 8.3304
5408 7.7613 8.3020
5592 7.7167 8.2758
.0075
.0080
.0085
.0090
.0095
40.29
41.51
42.67
43.76
44.81
1.0079
1.0084
1.0089
1.0094
1.0098
19 238
18 103
17099
16 203
15 399
168.78 2261.7 2430.5
173.87 2258.3 2432.2
178.69 2255.0 2433.7
183.27 2251.9 2435.2
187.64 2248.9 2436.6
168.79 2406.0 2574.8
173.88 2403.1 2577.0
178.70 2400.3 2579.0
183.29 2397.7 2581.0
187.65 2395.2 2582.9
5764 7.6750 8.2515
5926 7.6361 8.2287
6079 7.5994 8.2073
6224 7.5648 8.1872
.6362 7.5321 8.1682
.010
.011
.012
.013
.014
45.81
47.69
49.42
51.04
52.55
1.0102
10111
1.0119
1.0126
1.0134
14 674
13 415
12 361
il 465
10 693
191.82 2246.1 2437.9
199.66 2240.8 2440.4
206.91 2235,8 2442.7
213.66 2231.2 2444.9
219.98 2226.9 2446.9
191.83 2392.8 2584.7
199.67 2388.3 2588.0
206.92 2384.1 2591.1
213.67 2380.2 2593.9
219.99 2376.6 2596.6
.6493 7.5009 8.1502
6738 7.4430 8.1168
.6963 7.3900 8.0863
.7172 7.3412 8.0584
.7366 7.2959 8.0325
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