A rigid 14-L vessel initially contains a mixture of liquid water and vapor at 100°C with 12.3 percent quality. The mixture is then heated until its temperature is 180°C. The final state is superheated water and the internal energy at this state should be obtained by interpolation. Calculate the heat transfer required for this process. Use data from the steam tables. Water 100°C x = 0.123 The heat transfer required for this process is kJ.

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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890
PROPERTY TABLES AND CHARTS
TABLE A-5
Saturated water–Pressure table
Specific volume
m'/kg
Internal energy,
Enthalpy,
kJ/kg
Entropy,
kJ/kg-K
kJ/kg
St.
liquid, Evap., vapor,
h,
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
St.
Press.,
liquid, Evap., vapor,
temp., liquid,
T "C v,
vapor,
liquid, Evap.,
vapor,
P kPa
U,
1.0
6.97
13.02
0.001000 129.19
29.302 2355.2 2384.5
29.303 2484.4
2513.7
2524.7
0.1059
8.8690
8.9749
8.8270
8.7227
8.6421
1.5
0.001001 87.964
54.686 2338.1 2392.8
54.688
2470.1
0.1956
8.6314
2.0
2.5
17.50
21.08
0.001001 66.990
0.001002 54.242
73.431 2325.5 2398.9
88.422 2315.4 2403.8
73.433 2459.5 2532.9
88.424
0.2606 8.4621
2451.0 2539.4
0.3118 8.3302
3.0
24.08
0.001003 45.654
100.98
2306.9 2407.9
100.98
2443.9
2544.8
0.3543 8.2222 8.5765
4.0
28.96
0.001004 34.791
0.001005 28.185
0.001008 19.233
121.39 2293.1 2414.5
121.39 2432.3 2553.7
0.4224 8.0510
8.4734
5.0
7.5
32.87
40.29
137.75
168.74
2282.1 2419.8
2261.1 2429.8
137.75
168.75 2405.3
2423.0 2560.7
2574.0
0.4762 7.9176
0.5763 7.6738
8.3938
8.2501
10
45.81
53.97
0.001010 14.670
191.79 2245.4 2437.2
191.81
2392.1
2583.9
0.6492 7.4996
8.1488
15
0.001014 10.020
225.93
2222.1
2448.0
225.94 2372.3 2598.3
0.7549 7.2522
8.0071
20
25
60.06
64.96
0.001017 7.6481
0.001020 6.2034
251.40
271.93
2204.6 2456.0
2190.4 2462.4
251.42
271.96 2345.5
2357.5 2608.9
2617.5
0.8320 7.0752
0.8932 6.9370
7.9073
7.8302
30
69.09
0.001022 5.2287
289.24 2178.5 2467.7
289.27
2335.3 2624.6
0.9441 6.8234
7.7675
40
75.86
0.001026 3.9933
317.58
2158.8 2476.3
317.62 2318.4 2636.1
1.0261 6.6430
7.6691
50
81.32
0.001030 3.2403
340.49
2142.7 2483.2
340.54
2304.7
2645.2
1.0912 6.5019
7.5931
75
91.76
0.001037 2.2172
384.36 2111.8
2496.1
384.44
2278.0 2662.4
1.2132 6.2426
7.4558
100
0.001043 1.6941
99.61
101.325 99.97
105.97
111.35
417.40
2088.2 2505.6
417.51
2257.5 2675.0
1.3028 6.0562
7.3589
0.001043 1.6734
418.95
2087.0 2506.0
419.06 2256.5 2675.6
1.3069 6.0476
7.3545
1.3741
125
150
0.001048 1.3750
0.001053 1.1594
444.23
466.97
2068.8 2513.0
444.36
467.13
2240.6
2684.9
2226.0 2693.1
5.9100
7.2841
7.2231
2052.3 2519.2
1.4337 5.7894
175
116.04
0.001057 1.0037
486.82 2037.7 2524.5
487.01
2213.1
2700.2
1.4850 5.6865 7.1716
200
120.21
0.001061 0.88578
504.50
2024.6 2529.1
504.71
2201.6 2706.3
1.5302 5.5968
7.1270
225
250
123.97
127.41
130.58
0.001064 0.79329
520.47
535.08
548,57
2012.7 2533.2
2001.8 2536.8
520.71
2191.0
2711.7
2181.2 2716.5
1.5706 5.5171
7.0877
0.001067 0.71873
535.35
1.6072 5.4453
7.0525
275
0.001070 0.65732
1991.6 2540.1
548.86 2172.0 2720.9
1.6408 5.3800
7.0207
300
133.52
0.001073 0.60582
561.11
1982.1 2543.2
561.43 2163.5 2724.9
1.6717 5.3200
6.9917
325
350
136.27
138.86
0.001076 0.56199
0.001079 0.52422
572.84
583.89
1973.1 2545.9
1964.6 2548.5
573.19 2155.4
584.26 2147.7
2728.6
2732.0
1.7005 5.2645
1.7274 5.2128
6.9650
6.9402
141.30
1.7526 5.1645
1.7765 5.1191
375
0.001081 0.49133
594.32
604.22
1956,6
2550.9
594.73 2140.4 2735.1
6.9171
400
143.61 0.001084 0.46242
1948.9 2553.1
604.66 2133.4 2738.1
6.8955
450
500
147.90
151.83
0.001088 0.41392
0.001093 0.37483
622.65
639.54
1934.5 2557.1
1921.2 2560.7
623.14 2120.3 2743.4
640.09
655.77
670.38
684.08
1.8205 5.0356
1.8604 4.9603
6.8561
6.8207
2108.0 2748.1
550
155.46
0.001097 0.34261
655.16
1908.8 2563.9
2096.6 2752.4
1.8970 4.8916
6.7886
6.7593
6.7322
0.001101 0.31560
600
650
158.83
161.98 0.001104 0.29260
669.72 1897.1 2566.8
1886.1
2085.8
2075.5
2756.2
2759.6
1.9308 4.8285
1.9623
4.7699
683.37
2569.4
697.00
709.24
700
164.95
0.001108 0.27278
696.23
1875.6 2571.8
2065.8 2762.8
1.9918 4.7153 6.7071
750
167.75
0.001111 0.25552
708.40
1865.6 2574.0
2056.4
2765.7
2.0195 4.6642
6.6837
Transcribed Image Text:890 PROPERTY TABLES AND CHARTS TABLE A-5 Saturated water–Pressure table Specific volume m'/kg Internal energy, Enthalpy, kJ/kg Entropy, kJ/kg-K kJ/kg St. liquid, Evap., vapor, h, Sat. Sat. Sat. Sat. Sat. Sat. Sat. St. Press., liquid, Evap., vapor, temp., liquid, T "C v, vapor, liquid, Evap., vapor, P kPa U, 1.0 6.97 13.02 0.001000 129.19 29.302 2355.2 2384.5 29.303 2484.4 2513.7 2524.7 0.1059 8.8690 8.9749 8.8270 8.7227 8.6421 1.5 0.001001 87.964 54.686 2338.1 2392.8 54.688 2470.1 0.1956 8.6314 2.0 2.5 17.50 21.08 0.001001 66.990 0.001002 54.242 73.431 2325.5 2398.9 88.422 2315.4 2403.8 73.433 2459.5 2532.9 88.424 0.2606 8.4621 2451.0 2539.4 0.3118 8.3302 3.0 24.08 0.001003 45.654 100.98 2306.9 2407.9 100.98 2443.9 2544.8 0.3543 8.2222 8.5765 4.0 28.96 0.001004 34.791 0.001005 28.185 0.001008 19.233 121.39 2293.1 2414.5 121.39 2432.3 2553.7 0.4224 8.0510 8.4734 5.0 7.5 32.87 40.29 137.75 168.74 2282.1 2419.8 2261.1 2429.8 137.75 168.75 2405.3 2423.0 2560.7 2574.0 0.4762 7.9176 0.5763 7.6738 8.3938 8.2501 10 45.81 53.97 0.001010 14.670 191.79 2245.4 2437.2 191.81 2392.1 2583.9 0.6492 7.4996 8.1488 15 0.001014 10.020 225.93 2222.1 2448.0 225.94 2372.3 2598.3 0.7549 7.2522 8.0071 20 25 60.06 64.96 0.001017 7.6481 0.001020 6.2034 251.40 271.93 2204.6 2456.0 2190.4 2462.4 251.42 271.96 2345.5 2357.5 2608.9 2617.5 0.8320 7.0752 0.8932 6.9370 7.9073 7.8302 30 69.09 0.001022 5.2287 289.24 2178.5 2467.7 289.27 2335.3 2624.6 0.9441 6.8234 7.7675 40 75.86 0.001026 3.9933 317.58 2158.8 2476.3 317.62 2318.4 2636.1 1.0261 6.6430 7.6691 50 81.32 0.001030 3.2403 340.49 2142.7 2483.2 340.54 2304.7 2645.2 1.0912 6.5019 7.5931 75 91.76 0.001037 2.2172 384.36 2111.8 2496.1 384.44 2278.0 2662.4 1.2132 6.2426 7.4558 100 0.001043 1.6941 99.61 101.325 99.97 105.97 111.35 417.40 2088.2 2505.6 417.51 2257.5 2675.0 1.3028 6.0562 7.3589 0.001043 1.6734 418.95 2087.0 2506.0 419.06 2256.5 2675.6 1.3069 6.0476 7.3545 1.3741 125 150 0.001048 1.3750 0.001053 1.1594 444.23 466.97 2068.8 2513.0 444.36 467.13 2240.6 2684.9 2226.0 2693.1 5.9100 7.2841 7.2231 2052.3 2519.2 1.4337 5.7894 175 116.04 0.001057 1.0037 486.82 2037.7 2524.5 487.01 2213.1 2700.2 1.4850 5.6865 7.1716 200 120.21 0.001061 0.88578 504.50 2024.6 2529.1 504.71 2201.6 2706.3 1.5302 5.5968 7.1270 225 250 123.97 127.41 130.58 0.001064 0.79329 520.47 535.08 548,57 2012.7 2533.2 2001.8 2536.8 520.71 2191.0 2711.7 2181.2 2716.5 1.5706 5.5171 7.0877 0.001067 0.71873 535.35 1.6072 5.4453 7.0525 275 0.001070 0.65732 1991.6 2540.1 548.86 2172.0 2720.9 1.6408 5.3800 7.0207 300 133.52 0.001073 0.60582 561.11 1982.1 2543.2 561.43 2163.5 2724.9 1.6717 5.3200 6.9917 325 350 136.27 138.86 0.001076 0.56199 0.001079 0.52422 572.84 583.89 1973.1 2545.9 1964.6 2548.5 573.19 2155.4 584.26 2147.7 2728.6 2732.0 1.7005 5.2645 1.7274 5.2128 6.9650 6.9402 141.30 1.7526 5.1645 1.7765 5.1191 375 0.001081 0.49133 594.32 604.22 1956,6 2550.9 594.73 2140.4 2735.1 6.9171 400 143.61 0.001084 0.46242 1948.9 2553.1 604.66 2133.4 2738.1 6.8955 450 500 147.90 151.83 0.001088 0.41392 0.001093 0.37483 622.65 639.54 1934.5 2557.1 1921.2 2560.7 623.14 2120.3 2743.4 640.09 655.77 670.38 684.08 1.8205 5.0356 1.8604 4.9603 6.8561 6.8207 2108.0 2748.1 550 155.46 0.001097 0.34261 655.16 1908.8 2563.9 2096.6 2752.4 1.8970 4.8916 6.7886 6.7593 6.7322 0.001101 0.31560 600 650 158.83 161.98 0.001104 0.29260 669.72 1897.1 2566.8 1886.1 2085.8 2075.5 2756.2 2759.6 1.9308 4.8285 1.9623 4.7699 683.37 2569.4 697.00 709.24 700 164.95 0.001108 0.27278 696.23 1875.6 2571.8 2065.8 2762.8 1.9918 4.7153 6.7071 750 167.75 0.001111 0.25552 708.40 1865.6 2574.0 2056.4 2765.7 2.0195 4.6642 6.6837
A rigid 14-L vessel initially contains a mixture of liquid water and vapor at 100°C with 12.3 percent quality. The mixture is then heated
until its temperature is 180°C. The final state is superheated water and the internal energy at this state should be obtained by
interpolation. Calculate the heat transfer required for this process. Use data from the steam tables.
Water
100°C
x = 0.123
The heat transfer required for this process is
Transcribed Image Text:A rigid 14-L vessel initially contains a mixture of liquid water and vapor at 100°C with 12.3 percent quality. The mixture is then heated until its temperature is 180°C. The final state is superheated water and the internal energy at this state should be obtained by interpolation. Calculate the heat transfer required for this process. Use data from the steam tables. Water 100°C x = 0.123 The heat transfer required for this process is
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