An Isobaric process is done on steam where it is heated to 200 C at 1.1 MPa. It was initially a kilogram of saturated liquid. Find the change in volume, change in internal energy, change in enthalpy, and change in entropy. (0.1848 m3, 1837.31 kJ, 2040.66 kJ, 4.4609 kJ/k) Table 3. Vapor 1.15 (186.07) p(t Sat.) 1.10 (184.09) 10v 10 . 6.5381 177.53 2586.4 2781.7 170.13 2587.7 2783.3 Sat. 6.5535 175 180 185 190 195 172.50 2567.9 2757.6 175.28 2578 2 27710 6.5300 178.02 2588.2 2784.0 6.3587 180.71 2598.I 2796.9 6.5866 183.36 2607.8 2809.5 6.6137 164.20 25648 2753.6 166.91 2573.2 2767.2 169.37 258S.5 2780.5 172.18 2595.3 2793.5 6.5603 174.75 2605.4 2806.4 6.4726 6.3028 6.3320 6.5004 6.5878 177.28 2615.1 2819.0 6.6146 179.77 2624.6 2831.4 200 205 210 215 220 185.97 2617.4 2822.0 6.6401 188.56 2626.8 2834.2 6.6659 191.11 2636.1 2846.3 6.6911 182.24 2634.0 2843.6 6.6661 193.63 2645.3 2858.3 6.7157 196.13 2654.3 2870.1 6.7398 6.6407 184.68 2643.3 2855.7 187.09 2652.5 2867.6 6.7154 6.6910 225 230 235 240 245 198.60 2663.3 2881.8 6.7634 201.05 2672.2 2893.4 6.7865 203.49 2681.0 2904.9 6.8093 205.90 2689.8 2916.3 208.30 2698.5 2927.6 189.47 2661.5 2879.4 6.7392 191.84 2670.5 2891.1 194.19 2679.4 2902.7 196.51 2688.2 2914.2 198.82 2697.0 2925.6 6.7625 6.7855 6.8080 6.8301 6.8316 6.8535 250 260 270 280 290 210.7 2707.1 2938.8 6.8751 215.4 2724.2 2961.1 220.1 2741.1 2983.2 6.9584 224.7 2757.9 3005.1 229.3 2774.6 3026.9 201.1 2705.7 2936.9 205.7 2722.9 2959.4 210.2 2739.9 2981.6 214.6 2756.8 3003. 219.0 2773.6 3025.4 6.8518 6.8943 6.9356 6.9757 7.0149 6.9174 6.9984 7.0373
An Isobaric process is done on steam where it is heated to 200 C at 1.1 MPa. It was initially a kilogram of saturated liquid. Find the change in volume, change in internal energy, change in enthalpy, and change in entropy. (0.1848 m3, 1837.31 kJ, 2040.66 kJ, 4.4609 kJ/k) Table 3. Vapor 1.15 (186.07) p(t Sat.) 1.10 (184.09) 10v 10 . 6.5381 177.53 2586.4 2781.7 170.13 2587.7 2783.3 Sat. 6.5535 175 180 185 190 195 172.50 2567.9 2757.6 175.28 2578 2 27710 6.5300 178.02 2588.2 2784.0 6.3587 180.71 2598.I 2796.9 6.5866 183.36 2607.8 2809.5 6.6137 164.20 25648 2753.6 166.91 2573.2 2767.2 169.37 258S.5 2780.5 172.18 2595.3 2793.5 6.5603 174.75 2605.4 2806.4 6.4726 6.3028 6.3320 6.5004 6.5878 177.28 2615.1 2819.0 6.6146 179.77 2624.6 2831.4 200 205 210 215 220 185.97 2617.4 2822.0 6.6401 188.56 2626.8 2834.2 6.6659 191.11 2636.1 2846.3 6.6911 182.24 2634.0 2843.6 6.6661 193.63 2645.3 2858.3 6.7157 196.13 2654.3 2870.1 6.7398 6.6407 184.68 2643.3 2855.7 187.09 2652.5 2867.6 6.7154 6.6910 225 230 235 240 245 198.60 2663.3 2881.8 6.7634 201.05 2672.2 2893.4 6.7865 203.49 2681.0 2904.9 6.8093 205.90 2689.8 2916.3 208.30 2698.5 2927.6 189.47 2661.5 2879.4 6.7392 191.84 2670.5 2891.1 194.19 2679.4 2902.7 196.51 2688.2 2914.2 198.82 2697.0 2925.6 6.7625 6.7855 6.8080 6.8301 6.8316 6.8535 250 260 270 280 290 210.7 2707.1 2938.8 6.8751 215.4 2724.2 2961.1 220.1 2741.1 2983.2 6.9584 224.7 2757.9 3005.1 229.3 2774.6 3026.9 201.1 2705.7 2936.9 205.7 2722.9 2959.4 210.2 2739.9 2981.6 214.6 2756.8 3003. 219.0 2773.6 3025.4 6.8518 6.8943 6.9356 6.9757 7.0149 6.9174 6.9984 7.0373
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
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Question
Transcribed Image Text:An Isobaric process is done on steam where it is heated to 200 C at 1.1
MPa. It was initially a kilogram of saturated liquid. Find the change in
volume, change in internal energy, change in enthalpy, and change in
entropy. (0.1848 m3, 1837.31 kJ, 2040.66 kJ, 4.4609 kJ/k)
Table 3. Vapor
p(t Sat.)
1.10 (184.09)
1.15 (186.07)
10
10 .
Sat.
177.53 2586.4 2781.7
6.5535
170.13 2587.7 27833
6.5381
175
180
185
190
195
172.50 2567.9 2737.6
L75.28 25782 2771.0
178.02 2588.2 2784.0
180.71 2598.1 2796.9
183.36 2607.8 2809.5 6.6137
164.20 25648 2753.6
166.91 2573.2 2767.2
169 37 258SS 2780.5
172.18 2595.5 2793.5
174.75 2605.4 2806.4
6.4726
6.3028
63320
6.5603
6.5878
6.5004
63300
6.5587
6.5866
200
205
210
215
220
185.97 2617.4 2822.0 6.6401
188.56 2626.8 2834.2 6.6659
191.11 2636.1 2846.3 6.6911
193.63 2645.3 2858.3 6.7157
196.13 2654.3 2870.1 6.7398
177.28 2615.1 2819.0
179.77 2624.6 2831.4
182.24 2634.0 2843.6
184.68 2643.3 2855.7
187.09 2652.5 2867.6 6.7154
6.6146
6.6407
6.6661
6.6910
225
230
235
240
245
198.60 2663.3 2881.8 6.7634
201.05 2672.2 2893.4 6.7865
203.49 2681.0 2904.9 6.8093
205.90 2689.8 2916.3
208.30 2698.5 2927.6
189.47 2661.5 2879.4 6.7392
191.84 2670.5 2891.1
194.19 2679.4 2902.7
196.51 2688.2 2914.2
198.82 2697.0 2925.6
6.7625
6.7855
6.8080
6.8301
6.8316
6.8535
250
260
270
280
290
210.7 2707.1 2938.8
215.4 2724.2 2961.1
220.1 2741.1 2983.2
224.7 2757.9 3005.1
229.3 2774.6 3026.9
6.8751
6.9174
6.9584
6.9984
7.0373
201.1 2705.7 2936.9
205.7 2722.9 2959.4
210.2 2739.9 2981.6
214.6 2756.8 3003.6
219.0 2773.6 3025.4
6.8518
6.8943
6.9356
6.9757
7.0149
Enthalpy
Entropy
Specific Volume
Sat,
Sat.
Liquid
Vapor
10v
10,
Internal Energy
Sat,
Liquid
Tep
Sat.
Vapor
Sat.
Liquid
Sat.
Vapor
Sat.
1Jquid
Sat.
Vapor
Evap.
Evap.
Evap.
Press
MP
h/
h
h,
u
u,
s,
708.64 1866.1 2574.7
109.47 2057.0 2766.4
2.0200 4.6647 6.6847
255.6
252.4 711.00 1864.2 2575.2 711.85 2055.2 2767.0 2.0253 4.6549 6.6802
249.3 713.34 1862.2 25S75.6 714.20 2053.4 2767.5 2.0306 4.6451 6.6758
246.3 715.66 1860.3 25576.0 716.52 2051.6 2768.1 2.0359 4.6355 6.6714
243.3
167.78 1.115
.75
.76
.77
.78
.79
168.32
L1121
168.86
1.1128
169.39
1.1135
169.91 11142
717.95 1858.5 2576.4 718.83 2049.8 2768.6
2.0411 4.6260 6.6670
240.4 720.22 1856.6 2576.8 721.11 2048.0 2769.1 2.0462 4.6166 6.6628
237.6 722.47 1854.7 2577.2 723,38 2046.3 2769,7 2.0513 4.6073 6.6585
82 171.46 LI161 234.9 724.70 1852.9 2577.6 725.62 2044,5 2770.2 2.0563 45981 6.6544
232.2 726.91 1851.1 2578.0 727.83 2042.8 2770.7 2.0612 4.5890 6.6502
730.04 20411 2771.2 2.0662 4.5800 6.6462
170.43 1.1148
170.95 1.1155
.80
.83 171.97 1.1168
.84
172.47 1.1174
229.5
729.10 1849.2 2578.3
732.22 2039.4 2771.6 2.0710 4.5711 6.6421
734.38 2037.7 2772.1 2.0758 4.5623 6.6381
736.52 2036.1 2772.6 2.0806 4.5536 6.6342
738.64 2034.4 2773.0 2.0853 4.5450 6.6303
2.0900 4.5364 6.6264
227.0 731.27 1847.4 2578.7
83
.86
.87
88
89
172.96 1,1181
173.46 1.1187 224.5 733.42 1845.7 2579.1
173.94 1.1193 222.0 735.55 1843.9 2579.4
174.43 1.1200
174.90 1.1206
219.6
217.3 739.75 1840.4 2580.1 740.75 2032.8 2773.5
737.66 1842.1 2579.8
215.0
175.38 1.1212
175.85 1.1218 212.7
176.31 1.1225
176.78 1:1231
177.24 1.1237
741.83 1838.6 2580.5
743.89 1836.9 2580.8
745.93 1835.2 2581.1
747.95 1833.5 2581.5
749.96 1831.8 2581.8
742.83 2031.1 2773.9
744.91 2029.5 2774.4 2.0992 4.5196 6.6188
746.96 2027.9 2774.8 2.1038 4.5113 6.6151
749.00 2026.3 2775.3
751.02 2024.7 2775.7
2.0946 4.5280 6.6226
.90
,91
.92
.93
.94
210.5
208.4
206.3
2.1083 4.5031 6.6114
2.1127 4.4950 6.6077
177.69 1.1243
178.14 1.1249
178.59 1.1255
179.03 1.1261
179.47 1.1267
204 2
202.2 753.93 1828.5 2582.4
200.2
198.2
196.3
751.95 1830.2 2582.1
.95
,96
97
.98
.99
755.89 1826.9 2582,7
757.84 1825.2 2583.1
759.77 1823.6 2583.4
753.02 2023.1 2776.1 2.1172 4.4869 6.6041
755.01 2021.5 2776.5 2.1215 4.4789 6.6005
756.98 2019.9 2776.9 2.1259 4.4710 6.5969
758.94 2018.4 2777.3 2.1302 4.4632 6.5934
760.88 2016.8 2777.7
2.1345 4.4555 6.5899
1.00
1.02
1.04
1.06
1,08
179.91 1.1273 194.44
180.77 1.1284 190.80
181.62 1.1296 187.30
182,46
183.28
761.68 1822.0 2583.6
765.47 1818.8 2584.2 766.63 2012.2 2778.9
769.21 1815.6 2584.8
772.89 1812.5 2585.4
776.52 1809.4 2585.9
762.81 2015.3 2778.1
770.38 2009.2 2779.6
774.08 2006.2 2780.3
777.74 2003.3 2781.0
2.1387 4.4478 6.5865
2.1471 4.4326 6.5796
2.1553 4.4177 6.5729
2.1634 4.4030 6.5664
2.1713 4.3886 6.5599
1.1308
1.1319
183.92
180.67
1.10
1.12
184.09
184.89
1.1330
1.1342
177.53
174.49
780.09 1806.3 2586.4
783.62 1803.3 2586.9
781.34 2000.4 2781.7
784.89 1997.5 2782.4
2.1792 4.3744 6.5536
2.1869 4.3605 6.5473
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