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Steam Pipe Capacity Table (DN 15 – DN 300)

This steam pipe capacity table gives the throughput in kg/h that each nominal diameter carries at a given gauge pressure and steam velocity. It is the first check before sizing a steam valve or a trap: the same DN carries several times more steam at 14 bar than at 0.4 bar.

Steam throughput in kg/h for nominal pipe diameters DN 15–300, at gauge pressures from 0.4 to 14 bar and steam velocities of 15, 25 and 40 m/s.

Pressure (bar) Speed (m/s) DN 15 DN 20 DN 25 DN 32 DN 40 DN 50 DN 65 DN 80 DN 100 DN 125 DN 150 DN 200 DN 250 DN 300
0.4 15 7 15 24 37 62 99 145 213 394 648 917 1606 2590 3678
25 10 25 40 62 92 162 265 384 675 972 1457 2806 4101 5935
40 17 35 64 102 142 265 403 576 1037 1670 2303 4318 6909 9500
0.7 15 7 16 25 40 59 109 166 250 431 680 1006 1708 2791 3852
25 12 25 45 72 100 182 287 430 716 1145 1575 2816 4629 6204
40 18 37 68 106 167 298 428 630 1108 1712 2417 4532 7251 10323
1.0 15 8 17 29 43 65 112 182 260 470 694 120 1864 2814 4045
25 12 26 48 72 100 193 300 445 730 1160 1660 3099 4869 6751
40 19 39 71 112 172 311 465 640 1150 1800 2500 4815 7333 10370
2.0 15 12 25 45 70 100 182 280 410 715 1125 1580 2814 4545 6277
25 19 43 70 115 162 295 428 656 1215 1755 2520 4815 7425 10575
40 30 64 115 178 275 475 745 1010 1895 2925 4175 7578 11997 16796
3.0 15 16 37 60 93 127 245 385 535 925 1505 2040 3983 6217 8743
25 26 56 100 152 225 425 632 910 1580 2480 3440 6779 10269 14316
40 41 87 157 250 357 595 1025 1460 2540 4050 5940 10476 16470 22950
4.0 15 19 42 70 108 156 281 432 635 1166 1685 2460 4618 7121 10358
25 30 63 115 180 270 450 742 1080 1980 2925 4225 7866 12225 17304
40 49 116 197 295 456 796 1247 1825 3120 4940 7050 12661 19663 27816
5.0 15 22 49 87 128 187 352 526 770 1295 2105 2835 5548 8586 11947
25 36 81 135 211 308 548 885 1265 2110 3540 5150 8865 12468 20051
40 59 131 225 338 495 855 1350 1890 3510 5400 7870 13760 23205 32244
6.0 15 26 59 105 153 225 425 632 925 1555 2525 3400 6654 10297 14328
25 43 97 162 253 370 658 1065 1520 2530 4250 6175 10629 17108 24042
40 71 157 270 405 595 1025 1620 2270 4210 6475 9445 16515 27849 38697
8.0 15 32 70 126 190 285 475 800 1125 1990 3025 4540 8042 12625 17728
25 54 122 205 320 465 810 1260 1870 3240 5220 7120 13140 21600 33210
40 84 192 327 510 730 1370 2065 3120 5135 8395 12470 21247 33669 46858
10.0 15 41 95 155 250 372 626 1012 1465 2495 3995 5860 9994 16172 22713
25 66 145 257 405 562 990 1530 2205 3825 6295 8995 15966 25860 35890
40 104 216 408 615 910 1635 2545 3600 6230 9880 14390 26621 41011 57560
14.0 15 50 121 205 310 465 810 1270 1870 3220 5215 7390 12921 20538 29016
25 85 195 331 520 740 1375 2080 3120 5200 8500 12560 21720 34139 47128
40 126 305 555 825 1210 2195 3425 4735 8510 13050 18630 35548 54883 76534

Higher velocities allow a smaller pipe but increase pressure drop, noise and erosion. 15–25 m/s is usual for saturated steam distribution; 40 m/s only for short runs.

How the Steam Pipe Capacity Table Is Built

Each figure is the pipe cross-section multiplied by the steam velocity and divided by the specific volume of saturated steam at that pressure. That last term is why the steam pipe capacity table climbs so steeply across the page: at 0.4 bar gauge saturated steam occupies about 1.24 m³/kg, while at 14 bar it occupies only 0.132 m³/kg. The same DN 50 line therefore carries roughly nine times the mass flow at 14 bar that it carries at 0.4 bar, at an identical velocity. Read the steam pipe capacity table at the pressure the line actually runs at, never at the boiler rating.

Which Velocity Column to Use

For saturated steam distribution, take the 15 or 25 m/s columns of the steam pipe capacity table. The 40 m/s column belongs to short runs and connections, where the pressure drop over the length is small enough to ignore. Dry superheated steam tolerates the higher figures better, because there are no water droplets in the flow. With saturated steam at 40 m/s any carried moisture reaches elbows and valve seats as a jet of droplets, and the capacity gained by choosing the smaller pipe is paid back in erosion within a few years.

The Table Assumes Dry Saturated Steam

Every value in the steam pipe capacity table is for dry saturated steam. Wet steam carries less energy per kilogram, so a line that matches the steam pipe capacity table on paper can still fail to deliver the heat the process needs. Where the supply is known to be wet, fit a separator and a trap set before the branch rather than opening out the pipe size: a larger pipe lowers the velocity and drops even more water out of suspension.

Warm-up Load Is Not Running Load

A cold steam main condenses a great deal of steam while it heats up — several times the running load for the first minutes. The steam pipe capacity table describes the running condition, so a line sized from it alone still needs drain points for the start-up condensate: at the foot of every riser, ahead of every control valve, and every 30 to 50 m along a horizontal run. Opening the isolating valve slowly matters as much as the diameter taken from the steam pipe capacity table; a full-bore valve snapped open on a cold main is the classic cause of water hammer.

Do Not Size the Valve From the Pipe

The steam pipe capacity table gives a pipe diameter, not a valve size. A control valve is sized from the required kg/h and the pressure drop available across it, and the answer is very often one or two sizes below the line. Fitting a line-size control valve because the steam pipe capacity table produced a DN 100 main leaves the valve throttling close to its seat, which is noisy and wears the trim quickly. Isolating valves are the opposite case: they should be full bore and line size, so that they add nothing to the drop the steam pipe capacity table assumes.

Check the Lowest Working Pressure

Plant pressure varies. If a main is reduced to 3 bar for part of the plant, the steam pipe capacity table has to be read again at 3 bar for that section, where the same diameter carries far less steam. Read against the reduced pressure, the steam pipe capacity table makes that shortfall obvious before it is built in. Sizing every branch from the boiler pressure is the most common way to end up with a starved user at the far end of an otherwise adequate system.

Related Steam Tables

The steam pipe capacity table answers the flow question; the property questions sit next to it. The steam saturation temperature table gives the temperature that belongs to each pressure, which in turn sets the flange class and the gasket and packing materials, while the saturated steam table gives the enthalpy needed to turn a heat duty into kg/h — the number the steam pipe capacity table needs before it can be used at all. For water and other liquids the equivalent chart is the recommended pipe flow velocity table.

Steam pipe capacity table for DN 15 to DN 300 at 0.4 to 14 bar — PDF preview
Steam capacity with respect to pipe diameters, 15/25/40 m/s.

Reference: IAPWS IF-97 — industrial formulation for the thermodynamic properties of water and steam

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