tank (kpa), and the volume of the tank and draw (P-h) digram. Saturated Table Sat. Sat. Sat. Sat. Sat. Sat. Sat. liquid, Evap., vapor, vapor, Temp., press., liquid, Sat. Sat. liquid, Evap., vapor, h₂ his liquid, V₂ Evap., vapor, U₁ 4₂ T°C $1 % Part kPa S $18 15 1.7057 0.001001 77.885 20 2.3392 0.001002 57.762 38.597 0.001026 4.1291 62.980 2332.5 2395.5 83.913 2318.4 2402.3 313.99 2161.3 2475.3 314.03 2131.9 2487.8 356.02 377.04 2117.0 2494.0 398.09 57,868 0.001032 2.8261 355.96 2.3593 376.97 62.982 2465.4 2528.3 83.915 2453.5 2537.4 2320.6 2634.6 2295.3 2651.4 2282.5 2659.6 2269.6 2667.6 2216.0 2698.6 2202.1 2706.0 0.2245 8.5559 8.7803 0.2955 8.3696 8.6661 1.0158 6.6555 7.6812 1.1346 6.4089 7.5435 1.1929 6.2853 7.4782 1.2504 6.1647 7.4151 1.4737 5.7092 7.1829 1.5279 5.6013 7.1292 Sat. Sat. 0.001036 70.183 84.609 0.001040 1.9808 398.00 21020 2500.1 169.18 0.001056 1.0360 482.42 2040.9 2523.3 482.59 198.67 0.001050 0.89133 503.60 2025.3 2528.9 503.81 Sat. Sat. Sat. Sat. Sat. Sat. Sat. temp., liquid, vapor, liquid, Evap., vapor, Evap., vapor, liquid, h₁ vapor, liquid, Evap., h₂ S₁ $12 Tat °C V V₂ U₂ Ug ha 5₁ 45.81 0.001010 14.670 53.97 0.001014 10.020 2.2172 91.76 0.001037 99.61 0.001043 1.6941 116.04 0.001057 120.21 0.001061 123.97 0.001064 147.90 0.001088 151.83 0.001093 155.46 0.001097 191.79 2245.4 2437.2 191.81 2222.1 225.93 2448.0 225.94 384.36 2111.8 2495.1 384.44 417.40 2088.2 2505.6 417.51 2524.5 487.01 2037.7 1.0037 486.82 2024.6 0.88578 504.50 2529.1 504.71 2012.7 0.79329 520.47 2533.2 520.71 1934.5 2557.1 623.14 0.41392 622.65 1921.2 0.37483 639.54 2560.7 640.09 1908.8 2563.9 655.77 0.34261 655.16 719.97 2576.0 720.87 731.00 1846.9 2577.9 731.95 741.55 1838.1 2579.6 742.56 2392.1 2583.9 0.6492 7.4996 8.1488 2372.3 2598.3 0.7549 7.2522 8.0071 2278.0 2662.4 1.2132 6.2426 7.4558 2257.5 2675.0 1.3028 6.0562 7.3589 2213.1 2700.2 1.4850 5.6855 7.1716 2201.6 2706.3 1.5302 5.5968 7.1270 2191.0 2711.7 1.5706 5.5171 7.0877 2120.3 2743.4 1.8205 5.0356 6.8561 2108.0 2748.1 1.8604 4.9603 6.8207 2096.6 2752.4 1.8970 4.8916 6.7886 2047.5 2768.3 2.0457 4.6160 6.6616 2038.8 2770.8 2.0705 4.5705 6.6409 2030.5 2773.0 2.0941 4.5273 6.6213 170.41 0.001115 0.24035 1856.1 172.94 0.001118 0.22690 175.35 0.001121 0.21489 V U h S V U h S m³/kg kJ/kg kJ/kg kJ/kg-K m³/kg kJ/kg kJ/kg kJ/kg-K P= 2.00 MPa (212.38°C) P-1.80 MPa (207.11°C) 0.11037 2597.3 2795.9 6.3775 0.09959 2599.1 2798.3 6.3390 4825 0.10381 2628.5 2836.1 6.4160 0.11678 2637.0 2847.2 6.8246 0.12551 2773.2 3024.2 6.7684 0.14025 2777.4 3029.9 0.15122 2945.9 3248.4 7.1292 0.16849 2948.3 3251.6 7.1814 0.19551 3118.5 3470.4 7.4845 0.17568 3116.9 3468.3 7.4337 75 85 90 95 15 20 ress., kPa 0 5 5 D 5 D 5 O O D D D D perheated water (Concluded) V U h S m³/kg kJ/kg kJ/kg kJ/kg-K P 1.60 MPa (201.37°C) 0.12374 2594.8 2792.8 6.4200 0.13293 2645.1 2857.8 6.5537 0.15866 2781.6 3035.4 6.8864 0.19007 2950.8 3254.9 7.2394 0.22029 3120.1 3472.6 7.5410 5 -0 0 00

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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Q1-a: A rigid tank contains 50 kg of saturated liquid water at 90°C. Determine the pressure in
the tank (kpa), and the volume of the tank and draw (P-h) digram.
Saturated Table
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
Temp.,
liquid,
liquid,
press.,
vapor,
liquid,
Evap., vapor,
h₂
U₂
Evap., vapor,
h₂
his
liquid, Evap., vapor,
5
T°C
$1
V₂
Pust kPa u
U₂
$18
0.2245 8.5559 8.7803
0.2955 8.3596 8.6661
15
1.7057 0.001001
77.885
57.762
62.982 2455.4 2528.3
83.915 2453.5 2537.4
2320.6 2634.6
62.980 2332.5 2395.5
83.913 2318.4 2402.3
313.99 2161.3 2475.3 314.03
20
2.3392 0.001002
0.001026
4.1291
2.8261
0.001032
2295.3
356.02
355.96
376.97
398.00
2131.9 2487.8
2117.0 2494.0
2651,4
2659.6
2269.6 2667.6
2282.5
0.001036 2.3593
1.9808
1.0360 482.42
0.001040
21020 2500.1
377.04
398.09
482.59
503.81
115
169.18
0.001056
2216.0 2698.6
2202.1 2706.0
1.0158 6.6555 7.6812
1.1346 6.4089 7.5435
1.1929 6.2853 7.4782
1.2504 6.1647 7.4151
1.4737 5.7092 7.1829
1.5279 5.6013 7.1292
Sat.
Sat. Sat.
vapor, liquid, Evap.,
5₁ $12
120
198.67
2040.9 2523.3
2025.3 2528.9
Sat.
0.001050
0.89133 503.60
Sat.
Sat.
Sat.
Sat.
liquid,
Sat.
liquid, Evap., vapor,
U₂
vapor,
Evap.,
vapor,
Press.,
temp., liquid,
V₁
PkPa
Tut °C
V₂
U₂
h₂
htz
h₂
S₁
10
191.79 2245.4
2222.1
225.93
15
75
91.76 0.001037
100
99.61 0.001043
175
200
116.04 0.001057
120.21 0.001061
123.97 0.001064
147.90 0.001088
151.83 0.001093
155.46 0.001097
225
2392.1 2583.9 0.6492 7.4996 8.1488
2372.3 2598.3 0.7549 7.2522 8.0071
2278.0 2662.4 1.2132 6.2426 7.4558
2257.5 2675.0 1.3028 6.0562 7.3589
2213.1 2700.2 1.4850 5.6855 7.1716
2201.6 2706.3 1.5302 5.5968 7.1270
2191.0 2711.7 1.5706 5.5171 7.0877
2120.3 2743.4 1.8205 5.0356 6.8551
2108.0 2748.1 1.8604 4.9603 6.8207
2096.6 2752.4 1.8970 4.8916 6.7886
45.81 0.001010 14.670
53.97 0.001014 10.020
2111.8
384.36
2.2172
417.40 2088.2
1.6941
486.82
1.0037
0.88578 504.50
0.79329 520.47
0.41392 622.65
0.37483 639.54
0.34261 655.16
719.97
0.24035
731.00
0.22690
0.21489
2437.2 191.81
2448.0 225.94
2496.1 384.44
2505.6 417.51
2037.7 2524.5 487.01
2024.6 2529.1 504.71
2012.7 2533.2 520.71
1934.5 2557.1 623.14
1921.2 2560.7 640.09
1908.8 2563.9 655.77
1856.1 2576.0 720.87
1846.9 2577.9 731.95
2579.6 742.56
450
500
550
800 170.41 0.001115
850 172.94 0.001118
175.35 0.001121
900
2047.5 2768.3 2.0457 4.6160 6.6616
2038.8 2770.8 2.0705 4.5705 6.6409
2030.5 2773.0 2.0941 4.5273 6.6213
741.55
1838.1
Superheated water (Concluded)
T
U
h
U
h
V
V
V
S
S
U
S
h
kJ/kg kJ/kg kJ/kg-K
°C
m³/kg kJ/kg kJ/kg kJ/kg-K m³/kg
kJ/kg-K m³/kg
kJ/kg kJ/kg
P= 1.80 MPa (207.11°C)
P= 1.60 MPa (201.37°C)
Sat.
0.12374 2594.8 2792.8 6.4200
0.13293 2645.1 2857.8 6.5537
6.8864
0.15866 2781.6 3035.4
7.2394
P= 2.00 MPa (212.38°C)
0.09959 2599.1 2798.3 6.3390
0.10381 2628.5 2836.1 6.4160
0.12551 2773.2 3024.2 6.7684
0.15122 2945.9 3248.4 7.1292
0.16849
0.19551 3118.5 3470.4 7.4845 0.17568 3116.9 3468.3 7.4337
0.11037 2597.3 2795.9 6.3775
6.4825
2847.2
0.11678 2637.0
6.8246
0.14025 2777.4
3029.9
0.19007 2950.8 3254.9
2948.3 3251.6
7.1814
0.22029 3120.1 3472.6
7.5410
75
85
90
95
225
300
400
500
38.597
57,868
70.183
84.609
Transcribed Image Text:Q1-a: A rigid tank contains 50 kg of saturated liquid water at 90°C. Determine the pressure in the tank (kpa), and the volume of the tank and draw (P-h) digram. Saturated Table Sat. Sat. Sat. Sat. Sat. Sat. Sat. Sat. Sat. Temp., liquid, liquid, press., vapor, liquid, Evap., vapor, h₂ U₂ Evap., vapor, h₂ his liquid, Evap., vapor, 5 T°C $1 V₂ Pust kPa u U₂ $18 0.2245 8.5559 8.7803 0.2955 8.3596 8.6661 15 1.7057 0.001001 77.885 57.762 62.982 2455.4 2528.3 83.915 2453.5 2537.4 2320.6 2634.6 62.980 2332.5 2395.5 83.913 2318.4 2402.3 313.99 2161.3 2475.3 314.03 20 2.3392 0.001002 0.001026 4.1291 2.8261 0.001032 2295.3 356.02 355.96 376.97 398.00 2131.9 2487.8 2117.0 2494.0 2651,4 2659.6 2269.6 2667.6 2282.5 0.001036 2.3593 1.9808 1.0360 482.42 0.001040 21020 2500.1 377.04 398.09 482.59 503.81 115 169.18 0.001056 2216.0 2698.6 2202.1 2706.0 1.0158 6.6555 7.6812 1.1346 6.4089 7.5435 1.1929 6.2853 7.4782 1.2504 6.1647 7.4151 1.4737 5.7092 7.1829 1.5279 5.6013 7.1292 Sat. Sat. Sat. vapor, liquid, Evap., 5₁ $12 120 198.67 2040.9 2523.3 2025.3 2528.9 Sat. 0.001050 0.89133 503.60 Sat. Sat. Sat. Sat. liquid, Sat. liquid, Evap., vapor, U₂ vapor, Evap., vapor, Press., temp., liquid, V₁ PkPa Tut °C V₂ U₂ h₂ htz h₂ S₁ 10 191.79 2245.4 2222.1 225.93 15 75 91.76 0.001037 100 99.61 0.001043 175 200 116.04 0.001057 120.21 0.001061 123.97 0.001064 147.90 0.001088 151.83 0.001093 155.46 0.001097 225 2392.1 2583.9 0.6492 7.4996 8.1488 2372.3 2598.3 0.7549 7.2522 8.0071 2278.0 2662.4 1.2132 6.2426 7.4558 2257.5 2675.0 1.3028 6.0562 7.3589 2213.1 2700.2 1.4850 5.6855 7.1716 2201.6 2706.3 1.5302 5.5968 7.1270 2191.0 2711.7 1.5706 5.5171 7.0877 2120.3 2743.4 1.8205 5.0356 6.8551 2108.0 2748.1 1.8604 4.9603 6.8207 2096.6 2752.4 1.8970 4.8916 6.7886 45.81 0.001010 14.670 53.97 0.001014 10.020 2111.8 384.36 2.2172 417.40 2088.2 1.6941 486.82 1.0037 0.88578 504.50 0.79329 520.47 0.41392 622.65 0.37483 639.54 0.34261 655.16 719.97 0.24035 731.00 0.22690 0.21489 2437.2 191.81 2448.0 225.94 2496.1 384.44 2505.6 417.51 2037.7 2524.5 487.01 2024.6 2529.1 504.71 2012.7 2533.2 520.71 1934.5 2557.1 623.14 1921.2 2560.7 640.09 1908.8 2563.9 655.77 1856.1 2576.0 720.87 1846.9 2577.9 731.95 2579.6 742.56 450 500 550 800 170.41 0.001115 850 172.94 0.001118 175.35 0.001121 900 2047.5 2768.3 2.0457 4.6160 6.6616 2038.8 2770.8 2.0705 4.5705 6.6409 2030.5 2773.0 2.0941 4.5273 6.6213 741.55 1838.1 Superheated water (Concluded) T U h U h V V V S S U S h kJ/kg kJ/kg kJ/kg-K °C m³/kg kJ/kg kJ/kg kJ/kg-K m³/kg kJ/kg-K m³/kg kJ/kg kJ/kg P= 1.80 MPa (207.11°C) P= 1.60 MPa (201.37°C) Sat. 0.12374 2594.8 2792.8 6.4200 0.13293 2645.1 2857.8 6.5537 6.8864 0.15866 2781.6 3035.4 7.2394 P= 2.00 MPa (212.38°C) 0.09959 2599.1 2798.3 6.3390 0.10381 2628.5 2836.1 6.4160 0.12551 2773.2 3024.2 6.7684 0.15122 2945.9 3248.4 7.1292 0.16849 0.19551 3118.5 3470.4 7.4845 0.17568 3116.9 3468.3 7.4337 0.11037 2597.3 2795.9 6.3775 6.4825 2847.2 0.11678 2637.0 6.8246 0.14025 2777.4 3029.9 0.19007 2950.8 3254.9 2948.3 3251.6 7.1814 0.22029 3120.1 3472.6 7.5410 75 85 90 95 225 300 400 500 38.597 57,868 70.183 84.609
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