(a) An incoming stream of 1500kmol/min consists of saturated water with 65% liquid water and 35% steam at 40 bars. This steam is heated at constant pressure to 600°C. Using the steam tables, what is the heat transfer requirement for this step in kW? (Note: Steam tables in the bottom page) (b) This steam is then compressed isothermally to steam at 200 bars in a second step. What is the heat transfer requirement for this step in kW?

Elements Of Electromagnetics
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Publisher:Sadiku, Matthew N. O.
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(a) An incoming stream of 1500kmol/min consists of saturated water with 65% liquid water and 35% steam at 40 bars. This steam is heated at constant pressure to 600°C. Using the steam tables, what is the heat transfer requirement for this step in kW? (Note: Steam tables in the bottom page)
(b) This steam is then compressed isothermally to steam at 200 bars in a second step. What is the heat transfer requirement for this step in kW?

 

 

TABLE B.7 Properties of Superheated Steam
P(har)
Sat'd
Water Steam
Sar'd
Temperature ("C)-
50
75
100
150
200
250
300
350
2595
260
2481
2689
2317
2784
2589
2880
2662
2978
2736
3077
2812
3177
(-)
2446
1918
1918
2880
2661
2688
2783
25848
24380
2593
2444
14.8
2640
240
297
2736
242
3077
2812
265
3177
(45.)
2516
2588
14.7
160
172
195
21.8
287
3406
2646.0
24840
2093
2092
3139
3139
2683
2512
270
256
2878
279
2735
483
3016
2811
3.29
3177
2889
3.75
(1.3)
3406
324
0.00103
341
389
435
3140
3139
3176
2889
287
1.0
417.5
2675.4
2093
2092
2676
2507
2776
2583
2875
2668
217
2975
2734
2.40
3014
2811
2.64
(96)
4175
25061
1.49
1.94
5.0
6401
2747.5
209.7
2092
3143
3138
4194
4188
632.2
2855
2643
0425
2961
2724
0474
3168
2883
057
(1518)
639.6
2560.2
280
0375
0.00101
0.00100
0.00104
0.0009
10
(1799)
7626
O 7615
27762
2582
G194
2101
2091
3147
313.7
419.7
4187
6325
6314
2827
2621
0206
2943
2710
0233
3052
2794
0258
3159
2876
0282
0.00100
20
(2124)
908.6
9062
27972
29982
211.0
209.0
0.00101
315.5
3115
2902
2679
3139
2862
0139
4205
6039
9502
4184
0.00104
2774
0125
A 107A
O 1024
200
26013
a0
212.7
208.6
3171
3130
a.00102
6343
6300
292
2727
0.088
334
(250.3)
1008
000125
2829
A 12137
O 12068
60
27850
29904
214.4
208.3
318.7
542
3046
275.6)
3126
000103
4173
0.00L04
6291
873
2668
2792
002
8 1317.1
O 1060
80
27599
2571.7
216.1
20.1
3203
3123
2990
2750
(295.0)
167
S459
10758
a00124
2593
A 140R0
O 19935
2727.7
2547.3
100
217A
207A
0.00101
638.1
6273
3229
13434
2926
2700
311.7
416.1
44.4
10734
0.00124
13294
0.00140
A 1611.0
O 1561
150
2615.0
24599
2221
2070
3260
1107
6413
6250
1086.2
1067.7
0.00123
13382
13176
2005
(e.1)
4147
841.0
2523
A 1865
O 17857
200
24184
2264
2063
645
106.7
1022
13343
(MS.7)
16471
1613.7
300.7
4132
837.7
0.0014
6229
005875
221.2P) A 2108
2282
2060
10T
10600
a00114 0.00122
331.7
435.7
2108
2017
6458
861.4
13328
1638.5
16003
3092
4128
0.002
0.00103
0.00125
437.8
412.1
0.0010
250
2307
205.7
0.00100
334.0
647.7
8628
1087.5
1087.0
1331.1
1297.5
16250
(-)
307
0.00101
0.00122
300
235.0
205.0
1387
3381
609
4108
16099
156.3
102.1
0.00121
0.00101
456
6643
611.0
S00
251.9
2024
3542
304.0
8754
819.7
10936
13237
1299.3
15763
4058
0009911
0.00100
a00102
000144
1000
(-)
2939
195
3943
29.
0.0002 a01000 000104
9085
795.3
1328.7
1207.1
000122
11130
15505
14190
5944
000L14
"Adapted from R. W. Haywood, Thermodynamic Tubles in S2 (Metric) Unita Cambridge University Pres, London, 1968.
Water is a liquid in the enclosed region between 50C and 350C A specific enthalpy (kkg), 0 = spocific internal energy
(Lkg), P = specific valame (m'kg). Note: klg x 04303 = Btu/h,
(continued)
Transcribed Image Text:TABLE B.7 Properties of Superheated Steam P(har) Sat'd Water Steam Sar'd Temperature ("C)- 50 75 100 150 200 250 300 350 2595 260 2481 2689 2317 2784 2589 2880 2662 2978 2736 3077 2812 3177 (-) 2446 1918 1918 2880 2661 2688 2783 25848 24380 2593 2444 14.8 2640 240 297 2736 242 3077 2812 265 3177 (45.) 2516 2588 14.7 160 172 195 21.8 287 3406 2646.0 24840 2093 2092 3139 3139 2683 2512 270 256 2878 279 2735 483 3016 2811 3.29 3177 2889 3.75 (1.3) 3406 324 0.00103 341 389 435 3140 3139 3176 2889 287 1.0 417.5 2675.4 2093 2092 2676 2507 2776 2583 2875 2668 217 2975 2734 2.40 3014 2811 2.64 (96) 4175 25061 1.49 1.94 5.0 6401 2747.5 209.7 2092 3143 3138 4194 4188 632.2 2855 2643 0425 2961 2724 0474 3168 2883 057 (1518) 639.6 2560.2 280 0375 0.00101 0.00100 0.00104 0.0009 10 (1799) 7626 O 7615 27762 2582 G194 2101 2091 3147 313.7 419.7 4187 6325 6314 2827 2621 0206 2943 2710 0233 3052 2794 0258 3159 2876 0282 0.00100 20 (2124) 908.6 9062 27972 29982 211.0 209.0 0.00101 315.5 3115 2902 2679 3139 2862 0139 4205 6039 9502 4184 0.00104 2774 0125 A 107A O 1024 200 26013 a0 212.7 208.6 3171 3130 a.00102 6343 6300 292 2727 0.088 334 (250.3) 1008 000125 2829 A 12137 O 12068 60 27850 29904 214.4 208.3 318.7 542 3046 275.6) 3126 000103 4173 0.00L04 6291 873 2668 2792 002 8 1317.1 O 1060 80 27599 2571.7 216.1 20.1 3203 3123 2990 2750 (295.0) 167 S459 10758 a00124 2593 A 140R0 O 19935 2727.7 2547.3 100 217A 207A 0.00101 638.1 6273 3229 13434 2926 2700 311.7 416.1 44.4 10734 0.00124 13294 0.00140 A 1611.0 O 1561 150 2615.0 24599 2221 2070 3260 1107 6413 6250 1086.2 1067.7 0.00123 13382 13176 2005 (e.1) 4147 841.0 2523 A 1865 O 17857 200 24184 2264 2063 645 106.7 1022 13343 (MS.7) 16471 1613.7 300.7 4132 837.7 0.0014 6229 005875 221.2P) A 2108 2282 2060 10T 10600 a00114 0.00122 331.7 435.7 2108 2017 6458 861.4 13328 1638.5 16003 3092 4128 0.002 0.00103 0.00125 437.8 412.1 0.0010 250 2307 205.7 0.00100 334.0 647.7 8628 1087.5 1087.0 1331.1 1297.5 16250 (-) 307 0.00101 0.00122 300 235.0 205.0 1387 3381 609 4108 16099 156.3 102.1 0.00121 0.00101 456 6643 611.0 S00 251.9 2024 3542 304.0 8754 819.7 10936 13237 1299.3 15763 4058 0009911 0.00100 a00102 000144 1000 (-) 2939 195 3943 29. 0.0002 a01000 000104 9085 795.3 1328.7 1207.1 000122 11130 15505 14190 5944 000L14 "Adapted from R. W. Haywood, Thermodynamic Tubles in S2 (Metric) Unita Cambridge University Pres, London, 1968. Water is a liquid in the enclosed region between 50C and 350C A specific enthalpy (kkg), 0 = spocific internal energy (Lkg), P = specific valame (m'kg). Note: klg x 04303 = Btu/h, (continued)
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