In a steam system with 9 bar gauge pressure the absolute pressure is 10 bar. If a pressure drop of 3.5 bar is acceptable and suitable for the steam consumer, the pressure coefficient Pcoef should be 18.4.
Select the pressure coefficient - Pcoef - column closest possible to the actual pressure coefficient calculated in step 1.
Follow the column down until reaching the appropriate actual flow value. Interpolate between values if necessary.
Go left in the table to find the actual flow factor Kv.
Kv | Steam Flow (kg/h) | |||||||||
---|---|---|---|---|---|---|---|---|---|---|
Pressure Coefficient - Pcoeff | ||||||||||
1 | 1.25 | 1.56 | 1.95 | 2.44 | 3.05 | 3.81 | 4.77 | 5.96 | 7.45 | |
0.01 | 0 | 0 | 0 | 0 | 0 | 1 | 1 | 1 | 1 | 1 |
0.02 | 0 | 1 | 1 | 1 | 1 | 1 | 1 | 1 | 1 | 1 |
0.02 | 1 | 1 | 1 | 1 | 1 | 1 | 1 | 2 | 2 | 2 |
0.03 | 1 | 1 | 1 | 1 | 2 | 2 | 2 | 2 | 3 | 3 |
0.05 | 2 | 2 | 2 | 2 | 3 | 3 | 3 | 4 | 4 | 4 |
0.08 | 2 | 3 | 3 | 3 | 4 | 4 | 5 | 5 | 6 | 7 |
0.11 | 4 | 4 | 5 | 5 | 6 | 6 | 7 | 8 | 9 | 10 |
0.17 | 5 | 6 | 7 | 8 | 8 | 9 | 11 | 12 | 13 | 15 |
0.26 | 8 | 9 | 10 | 11 | 13 | 14 | 16 | 18 | 20 | 22 |
0.38 | 12 | 14 | 15 | 17 | 19 | 21 | 24 | 27 | 30 | 33 |
0.58 | 18 | 20 | 23 | 26 | 29 | 32 | 36 | 40 | 45 | 50 |
0.86 | 27 | 31 | 34 | 38 | 43 | 48 | 54 | 60 | 67 | 75 |
1.3 | 41 | 46 | 51 | 57 | 64 | 72 | 80 | 90 | 100 | 112 |
2.0 | 62 | 69 | 77 | 86 | 96 | 108 | 120 | 135 | 151 | 168 |
2.9 | 93 | 103 | 116 | 129 | 145 | 162 | 181 | 202 | 226 | 253 |
4.4 | 139 | 155 | 174 | 194 | 217 | 242 | 271 | 303 | 339 | 379 |
6.6 | 208 | 233 | 260 | 291 | 325 | 364 | 407 | 455 | 508 | 568 |
9.9 | 312 | 349 | 390 | 436 | 488 | 546 | 610 | 682 | 763 | 853 |
14.8 | 468 | 524 | 586 | 655 | 732 | 818 | 915 | 1023 | 1144 | 1279 |
22.2 | 703 | 786 | 878 | 982 | 1098 | 1228 | 1373 | 1535 | 1716 | 1918 |
33.3 | 1054 | 1179 | 1318 | 1473 | 1647 | 1841 | 2059 | 2302 | 2574 | 2877 |
49.9 | 1581 | 1768 | 1976 | 2210 | 2471 | 2762 | 3088 | 3453 | 3860 | 4316 |
74.8 | 2372 | 2652 | 2965 | 3315 | 3706 | 4143 | 4632 | 5179 | 5790 | 6474 |
112 | 3558 | 3978 | 4447 | 4972 | 5559 | 6215 | 6948 | 7769 | 8686 | 9711 |
168 | 5336 | 5966 | 6671 | 7458 | 8338 | 9322 | 10423 | 11653 | 13028 | 14566 |
253 | 8005 | 8949 | 10006 | 11187 | 12507 | 13983 | 15634 | 17479 | 19543 | 21849 |
379 | 12007 | 13424 | 15009 | 16780 | 18761 | 20975 | 23451 | 26219 | 29314 | 32774 |
568 | 18010 | 20136 | 22513 | 25170 | 28141 | 31463 | 35177 | 39329 | 43971 | 49161 |
852 | 27016 | 30204 | 33769 | 37755 | 42212 | 47194 | 52765 | 58993 | 65956 | 73741 |
1278 | 40523 | 45307 | 50654 | 56633 | 63318 | 70791 | 79147 | 88489 | 98934 | 110612 |
For full table - rotate the screen!
Kv | Steam Flow (kg/h) | |||||||||
---|---|---|---|---|---|---|---|---|---|---|
Pressure Coefficient - Pcoeff | ||||||||||
9.31 | 11.6 | 14.5 | 18.2 | 22.7 | 28.4 | 35.5 | 44.4 | 55.5 | 69.4 | |
0.01 | 1 | 1 | 1 | 1 | 2 | 2 | 2 | 2 | 2 | 3 |
0.02 | 1 | 2 | 2 | 2 | 2 | 3 | 3 | 3 | 4 | 4 |
0.02 | 2 | 2 | 3 | 3 | 3 | 4 | 4 | 5 | 5 | 6 |
0.03 | 3 | 4 | 4 | 5 | 5 | 6 | 6 | 7 | 8 | 9 |
0.05 | 5 | 5 | 6 | 7 | 8 | 9 | 10 | 11 | 12 | 13 |
0.08 | 7 | 8 | 9 | 10 | 11 | 13 | 14 | 16 | 18 | 20 |
0.11 | 11 | 12 | 14 | 15 | 17 | 19 | 22 | 24 | 27 | 30 |
0.17 | 17 | 18 | 21 | 23 | 26 | 29 | 32 | 36 | 40 | 45 |
0.26 | 25 | 28 | 31 | 35 | 39 | 43 | 48 | 54 | 61 | 68 |
0.38 | 37 | 42 | 46 | 52 | 58 | 65 | 73 | 81 | 91 | 102 |
0.58 | 56 | 62 | 70 | 78 | 87 | 97 | 109 | 122 | 136 | 152 |
0.86 | 84 | 94 | 105 | 117 | 131 | 146 | 163 | 183 | 204 | 228 |
1.3 | 126 | 140 | 157 | 175 | 196 | 219 | 245 | 274 | 306 | 343 |
2.0 | 188 | 210 | 235 | 263 | 294 | 329 | 368 | 411 | 460 | 514 |
2.9 | 282 | 316 | 353 | 395 | 441 | 493 | 552 | 617 | 689 | 771 |
4.4 | 424 | 474 | 530 | 592 | 662 | 740 | 827 | 925 | 1034 | 1156 |
6.6 | 635 | 710 | 794 | 888 | 993 | 1110 | 1241 | 1388 | 1551 | 1734 |
9.9 | 953 | 1066 | 1191 | 1332 | 1489 | 1665 | 1862 | 2081 | 2327 | 2602 |
14.8 | 1430 | 1598 | 1787 | 1998 | 2234 | 2498 | 2792 | 3122 | 3491 | 3903 |
22.2 | 2145 | 2398 | 2681 | 2997 | 3351 | 3746 | 4189 | 4683 | 5236 | 5854 |
33.3 | 3217 | 3597 | 4021 | 4496 | 5026 | 5620 | 6283 | 7025 | 7854 | 8781 |
49.9 | 4825 | 5395 | 6032 | 6744 | 7540 | 8429 | 9424 | 10537 | 11781 | 13171 |
74.8 | 7238 | 8092 | 9047 | 10115 | 11309 | 12644 | 14137 | 15805 | 17671 | 19757 |
112 | 10857 | 12138 | 13571 | 15173 | 16964 | 18966 | 21205 | 23708 | 26506 | 29635 |
168 | 16285 | 18208 | 20357 | 22760 | 25446 | 28449 | 31808 | 35562 | 39759 | 44452 |
253 | 24428 | 27312 | 30535 | 34139 | 38169 | 42674 | 47711 | 53343 | 59639 | 66679 |
379 | 36642 | 40967 | 45803 | 51209 | 57254 | 64011 | 71567 | 80014 | 89459 | 100018 |
568 | 54963 | 61451 | 68704 | 76814 | 85880 | 96017 | 107350 | 120021 | 134188 | 150027 |
852 | 82445 | 92176 | 103056 | 115220 | 128820 | 144026 | 161025 | 180032 | 201282 | 225040 |
1278 | 123668 | 138265 | 154584 | 172831 | 193231 | 216038 | 241538 | 270048 | 301923 | 337560 |
For a pressure coefficient Pcoef = 18.2 and steam flow = 592 kg/h - the flow factor Kv is 4.4.
The tables above are based on the formula:
Kv = m / (31.7 (dP / v)1/2) (1)
where
m= steam flow (kg/h)
dP = pressure drop (bar)
v = specific volume of steam before control valve (m3/kg)
Steam Kv calculator based on eq. 1:
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