You have two phases of liquid and vapor (i.e., wet steam) at 250°C in a high-temperature high-pressure vessel, which contains 0.8 grams of vapor and 5 grams of liquid. What is the specific volume of the vapor (ml/g)? What is the total volume (mL) of the vessel? The vessel temperature was increased from 250°C to 280°C wile keeping the volume from part the same. What is the mass (grams) of liquid then? 978 Appendix A.III: The Thermodynamic Properties of Water and Steam faturated Steam: Temperature Table (Continued)

Elements Of Electromagnetics
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ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
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a) You have two phases of liquid and vapor (i.e., wet steam) at 250°C in a high-temperature
high-pressure vessel, which contains 0.8 grams of vapor and 5 grams of liquid. What is the
specific volume of the vapor (ml/g)?
b) What is the total volume (mL) of the vessel?
c) The vessel temperature was increased from 250°C to 280°C wile keeping the volume from part b
the same. What is the mass (grams) of liquid then?
978 Appendix A.III: The Thermodynamic Properties of Water and Steam
Saturated Steam: Temperature Table (Continued)
Specific Volume
Sat.
Liquid
VL
175
180
185
190
195
Temp
(°C)
T
200
205
210
215
220
225
230
235
240
245
250
255
260
265
270
275
280
285
290
295
300
305
310
315
320
330
340
350
360
370
Press.
(MPa)
P
0.8920
0.001 121
1.0021 0.001 127
0.001 134
1.1227
1.2544 0.001 141
1.3978 0.001 149
1.5538
0.001 157
1.7230
0.001 164
1.9062 0.001 173
2.104
0.001 181
2.318
0.001 190
2.548
0.001 199
2.795 0.001 209
3.060
0.001 219
3.344
0.001 229
3.648 0.001 240
3.973 0.001 251
4.319 0.001 263
4.688
5.081
5.499
5.942
6.412
6.909
7.436
7.993
8.581
9.202
9.856
10.547
11.274
12.845
14.586
16.513
18.651
21.03
374.14 22.09
V [=] m³/kg:
Sat.
Vapor
VV
0.2168
0.194 05
0.174 09
0.156 54
0.141 05
0.127 36
0.115 21
0.104 41
0.094 79
0.086 19
0.078 49
0.071 58
0.065 37
0.059 76
0.054 71
0.050 13
0.045 98
0.042 21
0.038 77
0.035 64
0.032 79
0.030 17
0.027 77
0.025 57
0.023 54
0.021 67
0.019 948
0.018 350
0.016 867
0.015 488
0.012 996
0.010 797
0.008 813
0.006 945
0.004 925
0.003 155
Internal Energy
Evap.
AU
0.001 740
0.001 893
0.002 213
0.003 155
Ú, H =] J/g=kJ/kg;
Sat.
Liquid
ÜL
740.17
1840.0
762.09 1821.6
784.10
1802.9
806.19
1783.8
828.37 1764.4
850.65 1744.7
873.04 1724.5
895.53 1703.9
918.14 1682.9
940.87 1661.5
963.73 1639.6
986.74 1617.2
1009.89 1594.2
1332.0
1359.3
1387.1
1415.5
1444.6
1505.3
1570.3
2601.1
0600 A
2602.4
2006
2603.3
066.78
966.78 1836.5 2803.3 2.5639 3.6863 6.2503
200:10
6000.0
2603.9
2000
2604.1
1033.21 1570.8 2604.0
1056.71 1546.7 2603.4
1080.39 1522.0 2602.4
1104.28 1496.7 2600.9
1128.39 1470.6 2599.0
1152.74 1443.9 2596.6
0.001 302
1177.36 1416.3 2593.7
1202.25
0.001 317
1387.9 2590.2
990.12 1813.8 2804.0 2.6099 3.6047 6.2146
000
1013.62 1790.5 2804.2 2.6558 3.5233 6.1791
1037.32 1766.5 2803.8 2.7015 3.4422 6.1437
1061.23 1741.7 2803.0 2.7472 3.3612 6.1083
1085.36 1716.2 2801.5 2.7927 3.2802 6.0730
1109.73 1689.8 2799.5 2.8383 3.1992 6.0375
1134.37 1662.5 2796.9 2.8838 3.1181 6.0019
1159.28 1634.4 2793.6 2.9294 3.0368 5.9662
1184.51 1605.2 2789.7 2.9751
2789.7 2.9751 2.9551 5.9301
1210.07 1574.9 2785.0 3.0208 2.8730 5.8938
0.001 276
0.001 289
0.001 332
1227.46 1358.7
2586.1
1235.99
1262.31
0.001 348
1253.00 1328.4
2581.4
0.001 366
1278.92 1297.1
2576.0
1305.2 1264.7 2569.9
1543.6 2779.6 3.0668 2.7903 5.8571
1511.0 2773.3 3.1130 2.7070 5.8199
1289.07 1477.1 2766.2 3.1594 2.6227 5.7821
1316.3 1441.8 2758.1 3.2062 2.5375 5.7437
1344.0 1404.9 2749.0 3.2534 2.4511 5.7045
1366.4 2738.7 3.3010 2.3633 5.6643
0.001 384
0.001 404
1231.0 2563.0
0.001 425
2555.2
1372.4
0.001 447
2546.4
1401.3
1326.0 2727.3 3.3493 2.2737 5.6230
0.001 472
2536.6
1431.0
0.001 499
2525.5
0.001 561
0.001 638
1461.5
2498.9 1525.3
2464.6 1594.2
2418.4 1670.6
2351.5 1760.5
2228.5 1890.5
2029.6 2099.3
1283.5 2714.5 3.3982 2.1821 5.5804
1238.6 2700.1 3.4480 2.0882 5.5362
1140.6 2665.9 3.5507 1.8909 5.4417
1027.9 2622.0 3.6594 1.6763 5.3357
893.4 2563.9 3.7777 1.4335 5.2112
720.5 2481.0 3.9147 1.1379 5.0526
441.6 2332.1 4.1106 .6865 4.7971
4.4298
2099.3 4.4298 0
0
1641.9
1725.2
1844.0
2029.6
1195.9
1159.4
1121.1
1080.9
993.7
894.3
776.6
626.3
384.5
0
Sat.
Vapor
ŮV
S [=] kJ/kg K
2580.2
2583.7
2587.0
2590.0
2592.8
2595.3
2597.5
2500 5
2599.5
Enthalpy
Sat.
Liquid Evap.
ĤL ΔΗ HV
Sat. Sat.
Vapor Liquid
SL
Entropy
Evap.
AS
Sat.
Vapor
Šv
741.17 2032.4 2773.6 2.0909 4.5347 6.6256
763.22 2015.0 2778.2 2.1396 4.4461 6.5857
785.37 1997.1 2782.4 2.1879 4.3586 6.5465
807.62 1978.8 2786.4 2.2359 4.2720 6.5079
829.98 1960.0 2790.0 2.2835 4.1863 6.4698
852.45 1940.7 2793.2 2.3309 4.1014 6.4323
875.04
6.3952
1921.0 2796.0 2.3780 4.0172
1900.7 2798.5 2.4248 3.9337 6.3585
907.76
897.76
920.62 1879.9 2800.5 2.4714 3.8507 6.3221
1959 E 2802 1
2802.1
943.62 1858.5
2802.1 2.5178 3.7683 6.2861
Transcribed Image Text:a) You have two phases of liquid and vapor (i.e., wet steam) at 250°C in a high-temperature high-pressure vessel, which contains 0.8 grams of vapor and 5 grams of liquid. What is the specific volume of the vapor (ml/g)? b) What is the total volume (mL) of the vessel? c) The vessel temperature was increased from 250°C to 280°C wile keeping the volume from part b the same. What is the mass (grams) of liquid then? 978 Appendix A.III: The Thermodynamic Properties of Water and Steam Saturated Steam: Temperature Table (Continued) Specific Volume Sat. Liquid VL 175 180 185 190 195 Temp (°C) T 200 205 210 215 220 225 230 235 240 245 250 255 260 265 270 275 280 285 290 295 300 305 310 315 320 330 340 350 360 370 Press. (MPa) P 0.8920 0.001 121 1.0021 0.001 127 0.001 134 1.1227 1.2544 0.001 141 1.3978 0.001 149 1.5538 0.001 157 1.7230 0.001 164 1.9062 0.001 173 2.104 0.001 181 2.318 0.001 190 2.548 0.001 199 2.795 0.001 209 3.060 0.001 219 3.344 0.001 229 3.648 0.001 240 3.973 0.001 251 4.319 0.001 263 4.688 5.081 5.499 5.942 6.412 6.909 7.436 7.993 8.581 9.202 9.856 10.547 11.274 12.845 14.586 16.513 18.651 21.03 374.14 22.09 V [=] m³/kg: Sat. Vapor VV 0.2168 0.194 05 0.174 09 0.156 54 0.141 05 0.127 36 0.115 21 0.104 41 0.094 79 0.086 19 0.078 49 0.071 58 0.065 37 0.059 76 0.054 71 0.050 13 0.045 98 0.042 21 0.038 77 0.035 64 0.032 79 0.030 17 0.027 77 0.025 57 0.023 54 0.021 67 0.019 948 0.018 350 0.016 867 0.015 488 0.012 996 0.010 797 0.008 813 0.006 945 0.004 925 0.003 155 Internal Energy Evap. AU 0.001 740 0.001 893 0.002 213 0.003 155 Ú, H =] J/g=kJ/kg; Sat. Liquid ÜL 740.17 1840.0 762.09 1821.6 784.10 1802.9 806.19 1783.8 828.37 1764.4 850.65 1744.7 873.04 1724.5 895.53 1703.9 918.14 1682.9 940.87 1661.5 963.73 1639.6 986.74 1617.2 1009.89 1594.2 1332.0 1359.3 1387.1 1415.5 1444.6 1505.3 1570.3 2601.1 0600 A 2602.4 2006 2603.3 066.78 966.78 1836.5 2803.3 2.5639 3.6863 6.2503 200:10 6000.0 2603.9 2000 2604.1 1033.21 1570.8 2604.0 1056.71 1546.7 2603.4 1080.39 1522.0 2602.4 1104.28 1496.7 2600.9 1128.39 1470.6 2599.0 1152.74 1443.9 2596.6 0.001 302 1177.36 1416.3 2593.7 1202.25 0.001 317 1387.9 2590.2 990.12 1813.8 2804.0 2.6099 3.6047 6.2146 000 1013.62 1790.5 2804.2 2.6558 3.5233 6.1791 1037.32 1766.5 2803.8 2.7015 3.4422 6.1437 1061.23 1741.7 2803.0 2.7472 3.3612 6.1083 1085.36 1716.2 2801.5 2.7927 3.2802 6.0730 1109.73 1689.8 2799.5 2.8383 3.1992 6.0375 1134.37 1662.5 2796.9 2.8838 3.1181 6.0019 1159.28 1634.4 2793.6 2.9294 3.0368 5.9662 1184.51 1605.2 2789.7 2.9751 2789.7 2.9751 2.9551 5.9301 1210.07 1574.9 2785.0 3.0208 2.8730 5.8938 0.001 276 0.001 289 0.001 332 1227.46 1358.7 2586.1 1235.99 1262.31 0.001 348 1253.00 1328.4 2581.4 0.001 366 1278.92 1297.1 2576.0 1305.2 1264.7 2569.9 1543.6 2779.6 3.0668 2.7903 5.8571 1511.0 2773.3 3.1130 2.7070 5.8199 1289.07 1477.1 2766.2 3.1594 2.6227 5.7821 1316.3 1441.8 2758.1 3.2062 2.5375 5.7437 1344.0 1404.9 2749.0 3.2534 2.4511 5.7045 1366.4 2738.7 3.3010 2.3633 5.6643 0.001 384 0.001 404 1231.0 2563.0 0.001 425 2555.2 1372.4 0.001 447 2546.4 1401.3 1326.0 2727.3 3.3493 2.2737 5.6230 0.001 472 2536.6 1431.0 0.001 499 2525.5 0.001 561 0.001 638 1461.5 2498.9 1525.3 2464.6 1594.2 2418.4 1670.6 2351.5 1760.5 2228.5 1890.5 2029.6 2099.3 1283.5 2714.5 3.3982 2.1821 5.5804 1238.6 2700.1 3.4480 2.0882 5.5362 1140.6 2665.9 3.5507 1.8909 5.4417 1027.9 2622.0 3.6594 1.6763 5.3357 893.4 2563.9 3.7777 1.4335 5.2112 720.5 2481.0 3.9147 1.1379 5.0526 441.6 2332.1 4.1106 .6865 4.7971 4.4298 2099.3 4.4298 0 0 1641.9 1725.2 1844.0 2029.6 1195.9 1159.4 1121.1 1080.9 993.7 894.3 776.6 626.3 384.5 0 Sat. Vapor ŮV S [=] kJ/kg K 2580.2 2583.7 2587.0 2590.0 2592.8 2595.3 2597.5 2500 5 2599.5 Enthalpy Sat. Liquid Evap. ĤL ΔΗ HV Sat. Sat. Vapor Liquid SL Entropy Evap. AS Sat. Vapor Šv 741.17 2032.4 2773.6 2.0909 4.5347 6.6256 763.22 2015.0 2778.2 2.1396 4.4461 6.5857 785.37 1997.1 2782.4 2.1879 4.3586 6.5465 807.62 1978.8 2786.4 2.2359 4.2720 6.5079 829.98 1960.0 2790.0 2.2835 4.1863 6.4698 852.45 1940.7 2793.2 2.3309 4.1014 6.4323 875.04 6.3952 1921.0 2796.0 2.3780 4.0172 1900.7 2798.5 2.4248 3.9337 6.3585 907.76 897.76 920.62 1879.9 2800.5 2.4714 3.8507 6.3221 1959 E 2802 1 2802.1 943.62 1858.5 2802.1 2.5178 3.7683 6.2861
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