5.) A kilogram of wet steam is taken as a sample for study. It has a pressure of 0.805 MPa and an enthalpy of 2287 kJ/kg. What is the moisture percentage of the steam? • 23.56% • 76.50% • 55.41% • 89.49% Internal Energy Sat, Liguid Enthalpy Net. Entropy Set. Liquid Specific Volume Sat Sal. Vaper Nat. Vat Sat. Vapor Sal. Te Liguid Liqund Eap. Evap Prest MP Vaper Evap. 10, 10, h/ h, 2.0200 4.6647 6.6847 LI121 2524 711.00 1864 2 2575.2 711.85 2055.2 2767.0 2.0253 4.6549 6.6802 249.3 713.34 1862.2 2575.6 714.20 2053.4 27675 2.0306 4.6451 6.6758 246.3 715.66 1860.3 2576.0 716.52 20516 2768.1 2.0359 4.6355 6.6714 2.0411 4.6260 6.6670 167.78 1.1I15 255.6 708.64 1866.1 2574.7 709.47 2057.0 2766 4 .75 .76 168.32 77 168.86 LI128 78 169 39 1.1135 .79 169.91 1J142 243.3 717.95 1858.S 2576.4 718.83 2049.8 2768.6 720.22 1856.6 2576.8 721.11 2048.0 2769.1 722.47 1854.7 2577.2 723.38 2046.3 2769.7 2.0513 4.6073 6.6585 724.70 1852.9 2577.6 726.91 1851.I 2578.0 727.83 2042.8 2770.7 2.0612 4.5890 6.6s02 729.10 1849.2 25783 2.0462 4.6166 6.6628 80 .81 82 .83 .84 170.43 1.1148 170.95 1.1155 171.46 1.1161 171.97 1.1168 172.47 1.1174 240.4 237.6 234.9 232.2 229.5 725.62 2044.5 2770.2 20563 4.5981 6.6544 730.04 2041.I 2771.2 2.0662 4.5800 6.6462 172.96 1.1181 173.46 1.1187 85 86 87 88 89 227.0 224.5 222.0 219.6 217.3 731.27 1847.4 2578.7 733.42 1845.7 2579.1 735.55 1843.9 2579.4 737.66 1842.1 2579.8 739.75 1840.4 2580.1 732.22 2039.4 2771.6 734.38 2037.7 2772.1 736.52 2036.I 2772.6 738.64 2034.4 2773.0 740.75 2032.8 2773.5 2.0710 4.5711 6.6421 2.0758 4.5623 6.6381 2.0806 4.5536 6.6342 2.0853 4.5450 6.6303 2.0900 4,5364 6,6264 173.94 1.1193 174.43 174.90 1,1200 1.1206

Elements Of Electromagnetics
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ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
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5.) A kilogram of wet steam is taken as a sample for study. It has a pressure
of 0.805 MPa and an enthalpy of 2287 kJ/kg. What is the moisture percentage
of the steam?
• 23.56%
• 76.50%
• 55.41%
• 89.49%
Internal Energy
Sat,
Liguid
Enthalpy
Net.
Entropy
Set.
Liquid
Specific Volume
Sat
Sal.
Vaper
Nat.
Vat
Sat.
Vapor
Sal.
Te
Liguid
Liqund
Eap.
Evap
Prest
MP
Vaper
Evap.
10,
10,
h/
h,
2.0200 4.6647 6.6847
LI121 2524 711.00 1864 2 2575.2 711.85 2055.2 2767.0 2.0253 4.6549 6.6802
249.3 713.34 1862.2 2575.6 714.20 2053.4 27675 2.0306 4.6451 6.6758
246.3 715.66 1860.3 2576.0 716.52 20516 2768.1 2.0359 4.6355 6.6714
2.0411 4.6260 6.6670
167.78 1.1I15
255.6 708.64 1866.1 2574.7 709.47 2057.0 2766 4
.75
.76 168.32
77 168.86 LI128
78 169 39 1.1135
.79
169.91 1J142
243.3
717.95 1858.S 2576.4
718.83 2049.8 2768.6
720.22 1856.6 2576.8 721.11 2048.0 2769.1
722.47 1854.7 2577.2 723.38 2046.3 2769.7 2.0513 4.6073 6.6585
724.70 1852.9 2577.6
726.91 1851.I 2578.0 727.83 2042.8 2770.7 2.0612 4.5890 6.6s02
729.10 1849.2 25783
2.0462 4.6166 6.6628
80
.81
82
.83
.84
170.43 1.1148
170.95 1.1155
171.46 1.1161
171.97 1.1168
172.47 1.1174
240.4
237.6
234.9
232.2
229.5
725.62 2044.5 2770.2 20563 4.5981 6.6544
730.04 2041.I 2771.2 2.0662 4.5800 6.6462
172.96 1.1181
173.46 1.1187
85
86
87
88
89
227.0
224.5
222.0
219.6
217.3
731.27 1847.4 2578.7
733.42 1845.7 2579.1
735.55 1843.9 2579.4
737.66 1842.1 2579.8
739.75 1840.4 2580.1
732.22 2039.4 2771.6
734.38 2037.7 2772.1
736.52 2036.I 2772.6
738.64 2034.4 2773.0
740.75 2032.8 2773.5
2.0710 4.5711 6.6421
2.0758 4.5623 6.6381
2.0806 4.5536 6.6342
2.0853 4.5450 6.6303
2.0900 4,5364 6,6264
173.94
1.1193
174.43
174.90
1,1200
1.1206
Transcribed Image Text:5.) A kilogram of wet steam is taken as a sample for study. It has a pressure of 0.805 MPa and an enthalpy of 2287 kJ/kg. What is the moisture percentage of the steam? • 23.56% • 76.50% • 55.41% • 89.49% Internal Energy Sat, Liguid Enthalpy Net. Entropy Set. Liquid Specific Volume Sat Sal. Vaper Nat. Vat Sat. Vapor Sal. Te Liguid Liqund Eap. Evap Prest MP Vaper Evap. 10, 10, h/ h, 2.0200 4.6647 6.6847 LI121 2524 711.00 1864 2 2575.2 711.85 2055.2 2767.0 2.0253 4.6549 6.6802 249.3 713.34 1862.2 2575.6 714.20 2053.4 27675 2.0306 4.6451 6.6758 246.3 715.66 1860.3 2576.0 716.52 20516 2768.1 2.0359 4.6355 6.6714 2.0411 4.6260 6.6670 167.78 1.1I15 255.6 708.64 1866.1 2574.7 709.47 2057.0 2766 4 .75 .76 168.32 77 168.86 LI128 78 169 39 1.1135 .79 169.91 1J142 243.3 717.95 1858.S 2576.4 718.83 2049.8 2768.6 720.22 1856.6 2576.8 721.11 2048.0 2769.1 722.47 1854.7 2577.2 723.38 2046.3 2769.7 2.0513 4.6073 6.6585 724.70 1852.9 2577.6 726.91 1851.I 2578.0 727.83 2042.8 2770.7 2.0612 4.5890 6.6s02 729.10 1849.2 25783 2.0462 4.6166 6.6628 80 .81 82 .83 .84 170.43 1.1148 170.95 1.1155 171.46 1.1161 171.97 1.1168 172.47 1.1174 240.4 237.6 234.9 232.2 229.5 725.62 2044.5 2770.2 20563 4.5981 6.6544 730.04 2041.I 2771.2 2.0662 4.5800 6.6462 172.96 1.1181 173.46 1.1187 85 86 87 88 89 227.0 224.5 222.0 219.6 217.3 731.27 1847.4 2578.7 733.42 1845.7 2579.1 735.55 1843.9 2579.4 737.66 1842.1 2579.8 739.75 1840.4 2580.1 732.22 2039.4 2771.6 734.38 2037.7 2772.1 736.52 2036.I 2772.6 738.64 2034.4 2773.0 740.75 2032.8 2773.5 2.0710 4.5711 6.6421 2.0758 4.5623 6.6381 2.0806 4.5536 6.6342 2.0853 4.5450 6.6303 2.0900 4,5364 6,6264 173.94 1.1193 174.43 174.90 1,1200 1.1206
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