This question requires the use of the Thermodynamic Property Tables supplied as additional material. A saturated mixture of 2 kg of liquid water and 0.7 kg of steam is heated at a constant pressure of 40 bar until its temperature reaches 300 °C. (a) Evaluate the temperature and the dryness fraction at the start of the process. (b) Given that the heat transfer to a system during a constant pressure process is equal to the increase in enthalpy of the system, calculate the heat transfer to the system in the process described above. (c) Finally, the system undergoes an isentropic process such that it finishes as a saturated liquid. Evaluate the temperature at this final state. (d) Sketch the two processes on a plot of temperature.v.specific entropy. Include on your sketch the two-phase region and the isobar passing through states 1 and 2.

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Question 1
This question requires the use of the Thermodynamic Property Tables supplied as
additional material.
A saturated mixture of 2 kg of liquid water and 0.7 kg of steam is heated at a constant
pressure of 40 bar until its temperature reaches 300 °C.
(a) Evaluate the temperature and the dryness fraction at the start of the process.
(b) Given that the heat transfer to a system during a constant pressure process is equal to
the increase in enthalpy of the system, calculate the heat transfer to the system in the
process described above.
(c) Finally, the system undergoes an isentropic process such that it finishes as a
saturated liquid. Evaluate the temperature at this final state.
(d) Sketch the two processes on a plot of temperature.v.specific entropy. Include on your
sketch the two-phase region and the isobar passing through states 1 and 2.
Transcribed Image Text:Question 1 This question requires the use of the Thermodynamic Property Tables supplied as additional material. A saturated mixture of 2 kg of liquid water and 0.7 kg of steam is heated at a constant pressure of 40 bar until its temperature reaches 300 °C. (a) Evaluate the temperature and the dryness fraction at the start of the process. (b) Given that the heat transfer to a system during a constant pressure process is equal to the increase in enthalpy of the system, calculate the heat transfer to the system in the process described above. (c) Finally, the system undergoes an isentropic process such that it finishes as a saturated liquid. Evaluate the temperature at this final state. (d) Sketch the two processes on a plot of temperature.v.specific entropy. Include on your sketch the two-phase region and the isobar passing through states 1 and 2.
10:19 Wed 9 Aug
6 of 32
Saturated Water and Steam
PT₁8
[bar] [C] [m³/kg)
SHABAN BEKAS JY SA MGA Orong Nan G NHUNG CHANG
99.6
102.3
1.5 111.4
121.8
123.3
2.7 130.0
131.2
170.4
217.2
221.8
233.8
237.4
240.9
244.2
247.3
250.3
[kJ/kg]
417 2506
429 2510
439
449
458
qmplus.qmul.ac.uk
2512
2515
5210
2519
2521
1021 2603
1054
1068
1082
[kJ/kg]
417 2258
1025
2675
2680
2683
268
20⁹0
22222
=====
9229
1.303 6.056
1.333
5 994
1.361
5.937
1.387
5.884
1.411
1.434
1.455
1.475
1.494
520
1.547
2.679
710
2.740
[kJ/kg K]
797
€200
5.789
5.747
5.707
5.669
2:00
5.564
5.419
9.368
5321
5.214
5.121
4.893
4.830
600
4.375
4.307
1185
4.130
4.078
3.541
3.482
3.426
3.373
ni 97%
7.359
7.327
7.298
1.211
7332
7.202
7.182
7137
7.111
7.081
7.040
7.015
6.993
6.941
6.897
6832
6.790
6.761
6.709
0.003
6.586
6.554
0.323
6.160
6445
6.422
0.700
6.340
6.305
6212
6.186
6.161
6.136
6.113
6.070
Transcribed Image Text:10:19 Wed 9 Aug 6 of 32 Saturated Water and Steam PT₁8 [bar] [C] [m³/kg) SHABAN BEKAS JY SA MGA Orong Nan G NHUNG CHANG 99.6 102.3 1.5 111.4 121.8 123.3 2.7 130.0 131.2 170.4 217.2 221.8 233.8 237.4 240.9 244.2 247.3 250.3 [kJ/kg] 417 2506 429 2510 439 449 458 qmplus.qmul.ac.uk 2512 2515 5210 2519 2521 1021 2603 1054 1068 1082 [kJ/kg] 417 2258 1025 2675 2680 2683 268 20⁹0 22222 ===== 9229 1.303 6.056 1.333 5 994 1.361 5.937 1.387 5.884 1.411 1.434 1.455 1.475 1.494 520 1.547 2.679 710 2.740 [kJ/kg K] 797 €200 5.789 5.747 5.707 5.669 2:00 5.564 5.419 9.368 5321 5.214 5.121 4.893 4.830 600 4.375 4.307 1185 4.130 4.078 3.541 3.482 3.426 3.373 ni 97% 7.359 7.327 7.298 1.211 7332 7.202 7.182 7137 7.111 7.081 7.040 7.015 6.993 6.941 6.897 6832 6.790 6.761 6.709 0.003 6.586 6.554 0.323 6.160 6445 6.422 0.700 6.340 6.305 6212 6.186 6.161 6.136 6.113 6.070
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