Pls ASAP thanks in advance Question 1 This question requires the use of the Thermodynamic Property Tables supplied as additional material. A closed system comprises a rigid (non-deformable) vessel of volume 0.3 m3 containing 5 kg of pure water substance, initially at a pressure of 30 bar (state 1). (a) For state 1, show that the system is in the two phase region The system now undergoes an isochoric (constant volume) process during which its pressure increases to 70 bar (state 2). (b) For state 2 show that the system is now in the superheated region. (c) Sketch the process described above on a pressure v specific volume diagram. Include in your sketch the boundaries between the liquid, two phase and vapour regions, and the critical pressure.
Pls ASAP thanks in advance Question 1 This question requires the use of the Thermodynamic Property Tables supplied as additional material. A closed system comprises a rigid (non-deformable) vessel of volume 0.3 m3 containing 5 kg of pure water substance, initially at a pressure of 30 bar (state 1). (a) For state 1, show that the system is in the two phase region The system now undergoes an isochoric (constant volume) process during which its pressure increases to 70 bar (state 2). (b) For state 2 show that the system is now in the superheated region. (c) Sketch the process described above on a pressure v specific volume diagram. Include in your sketch the boundaries between the liquid, two phase and vapour regions, and the critical pressure.
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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Question
Pls ASAP thanks in advance
Question 1
This question requires the use of the Thermodynamic Property Tables supplied as
additional material.
A closed system comprises a rigid (non-deformable) vessel of volume 0.3 m3 containing 5
kg of pure water substance, initially at a pressure of 30 bar (state 1).
(a) For state 1, show that the system is in the two phase region
The system now undergoes an isochoric (constant volume) process during which its
pressure increases to 70 bar (state 2).
(b) For state 2 show that the system is now in the superheated region.
(c) Sketch the process described above on a pressure v specific volume diagram. Include
in your sketch the boundaries between the liquid, two phase and vapour regions, and
the critical pressure.
![P/[bar]
(T,/[°C])
(151.8)
6
(158.8)
7
(165.0)
8
(170.4)
9
(175.4)
10
(179.9)
15
(198.3)
20
(212.4)
30
(233.8)
40
(250.3)
50
(263.9)
60
(275.6)
70
(285.8)
h
S
0.3748
2562
2749
6.822
0.3156
2568
h2757
S 6.761
0.2728
2573
h2764
$6.709
0.2403
2577
2769
$6.663
D. 0.2149
4₂
2581
2774
S6.623
0.1944
2584
h 2778
S6.586
D 0.1317
42595
h 2792
S 6.445
D 0.0996
2600
h2799
S 6.340
D 0.0666
2603
h2803
S 6.186
D 0.0498
42602
h, 2801
6.070
0.0394
42597
h, 2794
$5.973
0.0324
42590
h₂ 2784
$ 5.890
%
0.0274
2581
h, 2772
S
*See footnote on p.6.
5.814
T
[°C]
V
u
h
S
D
u
h
S
u
h
S
V
U
h
S
V 0.3001
2636
2846
6.888
D
U
h
S
V
u
h
S
U
u
h
V
u
h
S
V
u
h
S
V
h
S
U
u
h
S
200
V
u
h
S
0.4252 0.4745 0.5226 0.5701
2804 2883
2644
2725
2857
2962
7.060
7.271
250 300 350
2835
6.753
0.3364
2720
2955
7.106
0.2061
2623
2829
6.695
3065 3168
7.460
7.633
0.3522 0.3940
0.4344
0.4743 0.5136 0.5528 0.5919
2881 2962 3044 3128
2640
2722
2801
2851
2958
3062
3166
3270
3376 3483
6.968
7.182 7.373 7.546
7.707
7.858 8.001
0.2610 0.2933 0.3242 0.3544
2631 2716 2798
2840
2951
7.040
6.817
r/[m³/kg]
u/(kJ/kg]
h/kJ/kg]
s/[kJ/kg k]
0.2305 0.2597 0.2874
2628
0.3714
2800
3060
7.298
0.0706
2646
2858
6.289
0.4058
2880
2961
3164 3269
7.473
7.634
3057 3162
7.233
400
2878 2960
3267
3160
7.352
0.6172
0.6641
3045 3129
0.7108 0.8040
2963
3300
3272 3377 3484 3702
7.793 7.944 8.087 8.351
0.4397 0.4734
3043
3374
7.786
7.409 7.571
0.0812 0.0905
2751
2845
2995
3117
6.541 6.744
Superheated Steam*
0.3842 0.4138
0.2328 0.2580
0.3065 0.3303 0.3540 0.4010
0.2825
2794 2875 2957
3040
3124 3297
3264 3370
3478 3698
8.028
2711
2944 3052 3158
6.926 7.124 7.301 7.464
0.1324 0.1520 0.1697 0.1865 0.2029 0.2191 0.2351 0.2667
2597 2697 2784 2868 2952 3035 3120 3294
3039 3148 3256 3364 3473 3694
6.919 7.102 7.268 7.423 7.569 7.838
2796
S 6.452
2925
6.711
450
0.3144 0.3410
2714 2796 2877 2959 3041
2948
3055
6.980 7.176
0.1115
0.1255 0.1386
2681
2774
2861
2904
3025
3138
6.547 6.768 6.957 7.126
500
2933
3231
6.921
0.3674 0.3937
3126
3266 3372 3480
7.515
7.667
7.811
3042 3126
3373
3481
7.723 7.866
0.0588
0.0664
2728
2828
2921
2963
3094
3214
6.364 6.584 6.769
0.4432
0.5069
0.5737
3127
3298
3482 3700
7.929
8.195
7.617 7.761
0.0993 0.1078 0.1161
3020 3108
3456
7.233
3343
7.082
600
0.1511 0.1634 0.1756 0.1995
2946 3030
3116
3291
3248
3357
3467
3690
7.283 7.431 7.701
0.6697
3299
3701
8.267
0.0733 0.0800 0.0864
0.5018
3298
3699
8.132
0.4458
3298
3699
8.077
0.0295 0.0352 0.0399 0.0441 0.0481
2634 2772 2879
2978
3073
2841 3018
3158
3287
3410
5.934
6.231
6.448 6.632
6.796
0.0988
3279
3010 3099
3330 3445 3674
0.0453 0.0519 0.0578
6.935 7.089 7.368
0.0632 0.0685 0.0786
3000 3090 3273
3316 3433 3666
2700
2810
2907
2927
3070
3196
6.212 6.451
6.646 6.818 6.975 7.258
0.1324
3285
3682
7.507
0.0362 0.0422 0.0473
2670 2792 2893
2887 3045 3177
0.0521 0.0566 0.0652
2988 3081
3266
3421
3657
3301
6.071 6.336 6.541 6.719 6.879 7.166
0.0556
3260
3649
7.088](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2Fc41f43b5-1aa0-491d-a8d1-548d7b858afd%2F07bc73a4-c913-4ec6-9b83-de01be906a5b%2Fnwhm4i8_processed.jpeg&w=3840&q=75)
Transcribed Image Text:P/[bar]
(T,/[°C])
(151.8)
6
(158.8)
7
(165.0)
8
(170.4)
9
(175.4)
10
(179.9)
15
(198.3)
20
(212.4)
30
(233.8)
40
(250.3)
50
(263.9)
60
(275.6)
70
(285.8)
h
S
0.3748
2562
2749
6.822
0.3156
2568
h2757
S 6.761
0.2728
2573
h2764
$6.709
0.2403
2577
2769
$6.663
D. 0.2149
4₂
2581
2774
S6.623
0.1944
2584
h 2778
S6.586
D 0.1317
42595
h 2792
S 6.445
D 0.0996
2600
h2799
S 6.340
D 0.0666
2603
h2803
S 6.186
D 0.0498
42602
h, 2801
6.070
0.0394
42597
h, 2794
$5.973
0.0324
42590
h₂ 2784
$ 5.890
%
0.0274
2581
h, 2772
S
*See footnote on p.6.
5.814
T
[°C]
V
u
h
S
D
u
h
S
u
h
S
V
U
h
S
V 0.3001
2636
2846
6.888
D
U
h
S
V
u
h
S
U
u
h
V
u
h
S
V
u
h
S
V
h
S
U
u
h
S
200
V
u
h
S
0.4252 0.4745 0.5226 0.5701
2804 2883
2644
2725
2857
2962
7.060
7.271
250 300 350
2835
6.753
0.3364
2720
2955
7.106
0.2061
2623
2829
6.695
3065 3168
7.460
7.633
0.3522 0.3940
0.4344
0.4743 0.5136 0.5528 0.5919
2881 2962 3044 3128
2640
2722
2801
2851
2958
3062
3166
3270
3376 3483
6.968
7.182 7.373 7.546
7.707
7.858 8.001
0.2610 0.2933 0.3242 0.3544
2631 2716 2798
2840
2951
7.040
6.817
r/[m³/kg]
u/(kJ/kg]
h/kJ/kg]
s/[kJ/kg k]
0.2305 0.2597 0.2874
2628
0.3714
2800
3060
7.298
0.0706
2646
2858
6.289
0.4058
2880
2961
3164 3269
7.473
7.634
3057 3162
7.233
400
2878 2960
3267
3160
7.352
0.6172
0.6641
3045 3129
0.7108 0.8040
2963
3300
3272 3377 3484 3702
7.793 7.944 8.087 8.351
0.4397 0.4734
3043
3374
7.786
7.409 7.571
0.0812 0.0905
2751
2845
2995
3117
6.541 6.744
Superheated Steam*
0.3842 0.4138
0.2328 0.2580
0.3065 0.3303 0.3540 0.4010
0.2825
2794 2875 2957
3040
3124 3297
3264 3370
3478 3698
8.028
2711
2944 3052 3158
6.926 7.124 7.301 7.464
0.1324 0.1520 0.1697 0.1865 0.2029 0.2191 0.2351 0.2667
2597 2697 2784 2868 2952 3035 3120 3294
3039 3148 3256 3364 3473 3694
6.919 7.102 7.268 7.423 7.569 7.838
2796
S 6.452
2925
6.711
450
0.3144 0.3410
2714 2796 2877 2959 3041
2948
3055
6.980 7.176
0.1115
0.1255 0.1386
2681
2774
2861
2904
3025
3138
6.547 6.768 6.957 7.126
500
2933
3231
6.921
0.3674 0.3937
3126
3266 3372 3480
7.515
7.667
7.811
3042 3126
3373
3481
7.723 7.866
0.0588
0.0664
2728
2828
2921
2963
3094
3214
6.364 6.584 6.769
0.4432
0.5069
0.5737
3127
3298
3482 3700
7.929
8.195
7.617 7.761
0.0993 0.1078 0.1161
3020 3108
3456
7.233
3343
7.082
600
0.1511 0.1634 0.1756 0.1995
2946 3030
3116
3291
3248
3357
3467
3690
7.283 7.431 7.701
0.6697
3299
3701
8.267
0.0733 0.0800 0.0864
0.5018
3298
3699
8.132
0.4458
3298
3699
8.077
0.0295 0.0352 0.0399 0.0441 0.0481
2634 2772 2879
2978
3073
2841 3018
3158
3287
3410
5.934
6.231
6.448 6.632
6.796
0.0988
3279
3010 3099
3330 3445 3674
0.0453 0.0519 0.0578
6.935 7.089 7.368
0.0632 0.0685 0.0786
3000 3090 3273
3316 3433 3666
2700
2810
2907
2927
3070
3196
6.212 6.451
6.646 6.818 6.975 7.258
0.1324
3285
3682
7.507
0.0362 0.0422 0.0473
2670 2792 2893
2887 3045 3177
0.0521 0.0566 0.0652
2988 3081
3266
3421
3657
3301
6.071 6.336 6.541 6.719 6.879 7.166
0.0556
3260
3649
7.088
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