3. A PVT cell containing pure water (H₂O) shows two equilibrium phases of vapor and liquid at 336.75°C. Answer the questions below by using Appendix A.III of Sandler, "steam table." What is the pressure (MPa) of the PVT cell? The visual window of the PVT cell shows 70 cm³ of vapor and 3 cm³ of liquid at What is the mass of water (a total of liquid water and vapor water) in the PVT cell? Since the water in the PVT cell shows two equilibrium phases at the temperature (and the corresponding pressure you answered in part a), it has no thermodynamic freedom (F = 0). When an additional heat is given to the system while keeping the temperature at 336.75°C and the pressure (that you answered in part a), the volume increases from 73 cm³ to 80 cm³. Note that the system is closed; hence, the total mass of water remains the same as Part b. What is the mass of liquid water, and what is the mass of vapor water? a. b. C. 336.75°C.
3. A PVT cell containing pure water (H₂O) shows two equilibrium phases of vapor and liquid at 336.75°C. Answer the questions below by using Appendix A.III of Sandler, "steam table." What is the pressure (MPa) of the PVT cell? The visual window of the PVT cell shows 70 cm³ of vapor and 3 cm³ of liquid at What is the mass of water (a total of liquid water and vapor water) in the PVT cell? Since the water in the PVT cell shows two equilibrium phases at the temperature (and the corresponding pressure you answered in part a), it has no thermodynamic freedom (F = 0). When an additional heat is given to the system while keeping the temperature at 336.75°C and the pressure (that you answered in part a), the volume increases from 73 cm³ to 80 cm³. Note that the system is closed; hence, the total mass of water remains the same as Part b. What is the mass of liquid water, and what is the mass of vapor water? a. b. C. 336.75°C.
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
Related questions
Question
Can u do part c? I would appreciate if u could check parts a and b too. Thanks
Transcribed Image Text:3.
A PVT cell containing pure water (H₂O) shows two equilibrium phases of vapor and
liquid at 336.75°C. Answer the questions below by using Appendix A.III of Sandler, "steam table."
What is the pressure (MPa) of the PVT cell?
The visual window of the PVT cell shows 70 cm³ of vapor and 3 cm³ of liquid at
What is the mass of water (a total of liquid water and vapor water) in the PVT cell?
Since the water in the PVT cell shows two equilibrium phases at the temperature
(and the corresponding pressure you answered in part a), it has no thermodynamic freedom
(F = 0). When an additional heat is given to the system while keeping the temperature at
336.75°C and the pressure (that you answered in part a), the volume increases from 73 cm³ to
80 cm³. Note that the system is closed; hence, the total mass of water remains the same as
Part b. What is the mass of liquid water, and what is the mass of vapor water?
a.
b.
C.
336.75°C.
![980 Appendix A.III: The Thermodynamic Properties of Water and Steam
Saturated Steam: Pressure Table (Continued)
Specific Volume
Sat.
Liquid
VL
Press. Temp
(MPa) (°C)
P
T
0.001 127
0.001 133
0.001 139
1.00 179.91
1.10 184.09
1.20 187.99
1.30 191.64 0.001 144
1.40 195.07 0.001 149
1.50 198.32 0.001 154
1.75 205.76 0.001 166
2.00 212.42
0.001 177
218.45
0.001 187
223.99
0.001 197
233.90 0.001 217
242.60
0.001 235
250.40
0.001 252
0.001 286
263.99
275.64 0.001 319
0.001 351
285.88
295.06
0.001 384
303.40
0.001 418
311.06
0.001 452
318.15
0.001 489
324.75 0.001 527
0.001 567
330.93
336.75
342.24 0.001 658
0.001 611
347.44 0.001 711
352.37
0.001 770
357.06
0.001 840
361.54
0.001 924
365.81 0.002 036
369.89 0.002 207
373.80
0.002 742
22.09 374.14 0.003 155
V [=] m³/kg;
2.25
2.5
3.00
3.5
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
Sat.
Vapor
VV
0.194 44
0.177 53
0.163 33
0.151 25
0.140 84
0.131 77
0.113 49
0.099 63
0.088 75
0.079 98
0.066 68
0.057 07
0.049 78
0.039 44
0.032 44
0.027 37
0.023 52
0.020 48
0.018 026
0.015 987
0.014 263
0.012 780
0.011 485
0.010 337
0.009 306
0.008 364
0.007 489
0.006 657
0.005 834
0.004 952
0.003 568
0.003 155
Û, Ĥ [=] J/g = kJ/kg;
Internal Energy
Sat.
Liquid
ÛL
Evap.
AU
Sat.
Vapor
ÛV
Sat.
Liquid
ĤL
Entropy
Sat.
Sat.
Sat.
Evap. Vapor
Liquid
Evap. Vapor
ΔΗ ĤV ŜL AS ŜV
Enthalpy
761.68
1822.0
2583.6
762.81
2015.3 2778.1
2000.4 2781.7
780.09
1806.3
2586.4 781.34
2.1387 4.4478
2.1792 4.3744
1986.2 2784.8 2.2166 4.3067
797.29 1791.5
2588.8
813.44 1777.5
2591.0
798.65
814.93 1972.7 2787.6
830.30 1959.7 2790.6
2.2515 4.2438
828.70 1764.1
6.4693
2592.8
2594.5
843.16
1751.3
6.4448
876.46
1721.4
2597.8
906.44 1693.8 2600.3
5.8133
5.7432
5.6772
2.2842 4.1850
844.89 1947.3 2792.2 2.3150 4.1298
878.50 1917.9 2796.4 2.3851 4.0044 6.3896
908.79 1890.7 2799.5 2.4474 3.8935 6.3409
933.83 1668.2 2602.0 936.49 1865.2 2801.7 2.5035 3.7937 6.2972
959.11
1644.0 2603.1 962.11 1841.0 2803.1 2.5547 3.7028 6.2575
1004.78 1599.3 2604.1 1008.42 1795.7 2804.2 2.6457 3.5412 6.1869
1045.43 1558.3 2603.7 1049.75 1753.7 2803.4 2.7253 3.4000 6.1253
1082.31 1520.0 2602.3 1087.31 1714.1 2801.4 2.7964 3.2737 6.0701
1147.81 1449.3 2597.1 1154.23 1640.1 2794.3 2.9202 3.0532 5.9734
1205.44 1384.3 2589.7 1213.35 1571.0 2784.3 3.0267 2.8625 5.8892
1257.55 1323.0 2580.5 1267.00 1505.1 2772.1 3.1211 2.6922
1305.57 1264.2 2569.8 1316.64 1441.3 2758.0 3.2068 2.5364
1350.51 1207.3 2557.8 1363.26 1378.9 2742.1 3.2858 2.3915
1393.04 1151.4 2544.4 1407.56
1096.0
2529.8 1450.1
1040.7 2513.7 1491.3
985.0 2496.1 1531.5
928.2 2476.8 1571.1
869.8 2455.5 1610.5
809.0 2431.7 1650.1
744.8 2405.0 1690.3
675.4 2374.3 1732.0
598.1 2338.1 1776.5
507.5 2293.0 1826.3
388.5 2230.6 1888.4
125.2 2087.1 2022.2
2029.6 2099.3
5.6141
3.4295 2.1233 5.5527
1433.7
1473.0
1511.1
1548.6
1585.6
1622.7
1660.2
1698.9
1739.9
1785.6
1842.1
1961.9
2029.6
1317.1 2724.7 3.3596 2.2544
1255.5 2705.6
1193.6 2684.9 3.4962 1.9962 5.4924
1130.7 2662.2 3.5606 1.8718 5.4323
1066.5 2637.6 3.6232 1.7485 5.3717
1000.0 2610.5 3.6848 1.6249 5.3098
930.6 2580.6 3.7461 1.4994 5.2455
856.9 2547.2 3.8079 1.3698 5.1777
777.1 2509.1 3.8715 1.2329 5.1044
688.0 2464.5 3.9388 1.0839 5.0228
583.4 2409.7 4.0139 0.9130 4.9269
446.2
143.4
2334.6 4.1075 0.6938 4.8013
2165.6 4.3110 0.2216 4.5327
0.0
0.0
2099.3 4.4298 0.0
4.4298
Ŝ [=] kJ/kg K
6.5865
6.5536
6.5233
6.4953](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F826dc16e-f1f4-4a8d-8075-483d691ac0ec%2Fadb1ca2e-4afc-43ff-b0f8-195922fe0485%2Fr8wqith_processed.jpeg&w=3840&q=75)
Transcribed Image Text:980 Appendix A.III: The Thermodynamic Properties of Water and Steam
Saturated Steam: Pressure Table (Continued)
Specific Volume
Sat.
Liquid
VL
Press. Temp
(MPa) (°C)
P
T
0.001 127
0.001 133
0.001 139
1.00 179.91
1.10 184.09
1.20 187.99
1.30 191.64 0.001 144
1.40 195.07 0.001 149
1.50 198.32 0.001 154
1.75 205.76 0.001 166
2.00 212.42
0.001 177
218.45
0.001 187
223.99
0.001 197
233.90 0.001 217
242.60
0.001 235
250.40
0.001 252
0.001 286
263.99
275.64 0.001 319
0.001 351
285.88
295.06
0.001 384
303.40
0.001 418
311.06
0.001 452
318.15
0.001 489
324.75 0.001 527
0.001 567
330.93
336.75
342.24 0.001 658
0.001 611
347.44 0.001 711
352.37
0.001 770
357.06
0.001 840
361.54
0.001 924
365.81 0.002 036
369.89 0.002 207
373.80
0.002 742
22.09 374.14 0.003 155
V [=] m³/kg;
2.25
2.5
3.00
3.5
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
Sat.
Vapor
VV
0.194 44
0.177 53
0.163 33
0.151 25
0.140 84
0.131 77
0.113 49
0.099 63
0.088 75
0.079 98
0.066 68
0.057 07
0.049 78
0.039 44
0.032 44
0.027 37
0.023 52
0.020 48
0.018 026
0.015 987
0.014 263
0.012 780
0.011 485
0.010 337
0.009 306
0.008 364
0.007 489
0.006 657
0.005 834
0.004 952
0.003 568
0.003 155
Û, Ĥ [=] J/g = kJ/kg;
Internal Energy
Sat.
Liquid
ÛL
Evap.
AU
Sat.
Vapor
ÛV
Sat.
Liquid
ĤL
Entropy
Sat.
Sat.
Sat.
Evap. Vapor
Liquid
Evap. Vapor
ΔΗ ĤV ŜL AS ŜV
Enthalpy
761.68
1822.0
2583.6
762.81
2015.3 2778.1
2000.4 2781.7
780.09
1806.3
2586.4 781.34
2.1387 4.4478
2.1792 4.3744
1986.2 2784.8 2.2166 4.3067
797.29 1791.5
2588.8
813.44 1777.5
2591.0
798.65
814.93 1972.7 2787.6
830.30 1959.7 2790.6
2.2515 4.2438
828.70 1764.1
6.4693
2592.8
2594.5
843.16
1751.3
6.4448
876.46
1721.4
2597.8
906.44 1693.8 2600.3
5.8133
5.7432
5.6772
2.2842 4.1850
844.89 1947.3 2792.2 2.3150 4.1298
878.50 1917.9 2796.4 2.3851 4.0044 6.3896
908.79 1890.7 2799.5 2.4474 3.8935 6.3409
933.83 1668.2 2602.0 936.49 1865.2 2801.7 2.5035 3.7937 6.2972
959.11
1644.0 2603.1 962.11 1841.0 2803.1 2.5547 3.7028 6.2575
1004.78 1599.3 2604.1 1008.42 1795.7 2804.2 2.6457 3.5412 6.1869
1045.43 1558.3 2603.7 1049.75 1753.7 2803.4 2.7253 3.4000 6.1253
1082.31 1520.0 2602.3 1087.31 1714.1 2801.4 2.7964 3.2737 6.0701
1147.81 1449.3 2597.1 1154.23 1640.1 2794.3 2.9202 3.0532 5.9734
1205.44 1384.3 2589.7 1213.35 1571.0 2784.3 3.0267 2.8625 5.8892
1257.55 1323.0 2580.5 1267.00 1505.1 2772.1 3.1211 2.6922
1305.57 1264.2 2569.8 1316.64 1441.3 2758.0 3.2068 2.5364
1350.51 1207.3 2557.8 1363.26 1378.9 2742.1 3.2858 2.3915
1393.04 1151.4 2544.4 1407.56
1096.0
2529.8 1450.1
1040.7 2513.7 1491.3
985.0 2496.1 1531.5
928.2 2476.8 1571.1
869.8 2455.5 1610.5
809.0 2431.7 1650.1
744.8 2405.0 1690.3
675.4 2374.3 1732.0
598.1 2338.1 1776.5
507.5 2293.0 1826.3
388.5 2230.6 1888.4
125.2 2087.1 2022.2
2029.6 2099.3
5.6141
3.4295 2.1233 5.5527
1433.7
1473.0
1511.1
1548.6
1585.6
1622.7
1660.2
1698.9
1739.9
1785.6
1842.1
1961.9
2029.6
1317.1 2724.7 3.3596 2.2544
1255.5 2705.6
1193.6 2684.9 3.4962 1.9962 5.4924
1130.7 2662.2 3.5606 1.8718 5.4323
1066.5 2637.6 3.6232 1.7485 5.3717
1000.0 2610.5 3.6848 1.6249 5.3098
930.6 2580.6 3.7461 1.4994 5.2455
856.9 2547.2 3.8079 1.3698 5.1777
777.1 2509.1 3.8715 1.2329 5.1044
688.0 2464.5 3.9388 1.0839 5.0228
583.4 2409.7 4.0139 0.9130 4.9269
446.2
143.4
2334.6 4.1075 0.6938 4.8013
2165.6 4.3110 0.2216 4.5327
0.0
0.0
2099.3 4.4298 0.0
4.4298
Ŝ [=] kJ/kg K
6.5865
6.5536
6.5233
6.4953
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