Steam Flow Rate Pipes
Reference data and engineering information about steam flow rate pipes for fluid mechanics applications.
Overview
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Steam flow rate data for Schedule 40 steel pipes, based on allowable pressure drops ranging from 1/16 to 2 psi per 100 ft of pipe. These values apply to saturated steam at low pressures (3–5 psig) and are used for sizing steam distribution piping in heating and process systems.
Selecting the right pipe size balances installation cost against acceptable pressure loss. Smaller pipes are cheaper but create higher pressure drops, while oversized pipes waste material and increase heat loss.
Original Source Scope
The source page title is Steam Flow Rate vs. Pressure Drop - Schedule 40 Pipe and its subtitle states that the data is flow rate (lb/h) and pressure drop per 100 feet of pipe. The original article text says that steam flow rates in Schedule 40 steel pipes are tabulated for pressure drops from 1/16 psi to 2 psi, and that wider screens show the full table with the higher pressure-drop columns.
Steam flow rates in schedule 40 steel pipes with pressure drops ranging 1/16 to 2 psi:
For full table with higher pressure drops - rotate the screen!
The source also includes three unit notes: 1 in = 25.4 mm, 1 ft = 0.3048 m, and 1 psi = 6895 Pa = 0.069 bar. Shared site navigation/search tables from the source extraction are intentionally excluded because they are not engineering data; the complete engineering data table is preserved below.
Key Formulas
The underlying flow relationship comes from the Darcy-Weisbach equation for pressure drop in straight pipe:
For sizing purposes, velocity can also be expressed through mass flow:
Typical steam velocities in distribution mains range from 4,000 to 6,000 ft/min (20–30 m/s), depending on operating pressure and pipe length.
Variables
| Symbol | Description | Unit |
|---|---|---|
| Pressure drop | psi | |
| Darcy friction factor | — | |
| Pipe length | ft | |
| Inside pipe diameter | ft or in | |
| Steam density | lb/ft³ | |
| Flow velocity | ft/min | |
| Mass flow rate | lb/h | |
| Cross-sectional area | ft² |
Restored Original Source Tables
The following tables are restored from the original source page to preserve the complete reference data.
Original Source Layout/Search Table
Column 1 | Column 2 | Column 3 | Column 4 | Column 5 |
|---|---|---|---|---|
| × | × | 検索 | ||
| × |
Source: engineeringtoolbox.com
Steam Flow Rate vs. Pressure Drop - Schedule 40 Pipe
Pressure drop per 100 ft of pipe length | Pressure drop per 100 ft of pipe length | Pressure drop per 100 ft of pipe length | Pressure drop per 100 ft of pipe length | Pressure drop per 100 ft of pipe length | Pressure drop per 100 ft of pipe length | Pressure drop per 100 ft of pipe length | Pressure drop per 100 ft of pipe length | Pressure drop per 100 ft of pipe length | Pressure drop per 100 ft of pipe length | Pressure drop per 100 ft of pipe length | Pressure drop per 100 ft of pipe length | Pressure drop per 100 ft of pipe length | Pressure drop per 100 ft of pipe length | Flow Rate (lb/h) |
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| 1/16 psi (1 oz/in2) | 1/16 psi (1 oz/in2) | 1/8 psi (2 oz/in2) | 1/8 psi (2 oz/in2) | 1/4 psi (4 oz/in2) | 1/4 psi (4 oz/in2) | 1/2 psi (8 oz/in2) | 1/2 psi (8 oz/in2) | 3/4 psi (12 oz/in2) | 3/4 psi (12 oz/in2) | 1 psi | 1 psi | 2 psi | 2 psi | |
| Saturated Pressure (psig) | Saturated Pressure (psig) | Saturated Pressure (psig) | Saturated Pressure (psig) | Saturated Pressure (psig) | Saturated Pressure (psig) | Saturated Pressure (psig) | Saturated Pressure (psig) | Saturated Pressure (psig) | Saturated Pressure (psig) | Saturated Pressure (psig) | Saturated Pressure (psig) | Saturated Pressure (psig) | Saturated Pressure (psig) | |
| 3.5 | 12 | 3.5 | 12 | 3.5 | 12 | 3.5 | 12 | 3.5 | 12 | 3.5 | 12 | 3.5 | 12 | |
| 3/4 | 9 | 11 | 14 | 16 | 20 | 24 | 29 | 35 | 36 | 43 | 42 | 50 | 60 | 73 |
| 1 | 17 | 21 | 26 | 31 | 37 | 46 | 54 | 66 | 68 | 82 | 81 | 93 | 114 | 137 |
| 1 1/4 | 36 | 45 | 53 | 66 | 78 | 96 | 111 | 138 | 140 | 170 | 162 | 200 | 232 | 280 |
| 1 1/2 | 56 | 70 | 84 | 100 | 120 | 147 | 174 | 210 | 218 | 260 | 246 | 304 | 360 | 430 |
| 2 | 108 | 134 | 162 | 194 | 234 | 285 | 336 | 410 | 420 | 510 | 480 | 590 | 710 | 850 |
| 2 1/2 | 174 | 215 | 258 | 310 | 378 | 460 | 540 | 660 | 680 | 820 | 780 | 950 | 1150 | 1370 |
| 3 | 318 | 380 | 465 | 550 | 660 | 810 | 960 | 1160 | 1190 | 1430 | 1380 | 1670 | 1950 | 2400 |
| 3 1/2 | 462 | 550 | 670 | 800 | 990 | 1218 | 1410 | 1700 | 1740 | 2100 | 2000 | 2420 | 2950 | 3450 |
| 4 | 640 | 800 | 950 | 1160 | 1410 | 1690 | 1980 | 2400 | 2450 | 3000 | 2880 | 3460 | 4200 | 4900 |
| 5 | 1200 | 1430 | 1680 | 2100 | 2440 | 3000 | 3570 | 4250 | 4380 | 5250 | 5100 | 6100 | 7500 | 8600 |
| 6 | 1920 | 2300 | 2820 | 3350 | 3960 | 4850 | 5700 | 6800 | 7000 | 8600 | 8400 | 10000 | 11900 | 14200 |
| 8 | 3900 | 4800 | 5570 | 7000 | 8100 | 10000 | 11400 | 14300 | 14500 | 17700 | 16500 | 20500 | 24000 | 29500 |
| 10 | 7200 | 8800 | 10200 | 12600 | 15000 | 18200 | 21000 | 26000 | 26200 | 32000 | 30000 | 37000 | 42700 | 52000 |
| 12 | 11400 | 13700 | 16500 | 19500 | 23400 | 28400 | 33000 | 40000 | 41000 | 49500 | 48000 | 57500 | 67800 | 81000 |
Source: engineeringtoolbox.com
Engineering Notes
Steam Flow Unit Converter
- Pressure drop basis. Values are per 100 ft of straight pipe. For longer runs, scale linearly or use the Darcy-Weisbach equation with appropriate friction factors.
- Higher pressures. At 5 psig saturated pressure, capacities increase roughly 20–25% compared to 3.5 psig for the same pipe size and pressure drop allowance.
- Fittings and valves. Add equivalent lengths of pipe for elbows, tees, and valves. A common rule is 50–75% additional length for typical distribution systems.
- Noise and erosion. Velocities above 6,000 ft/min (30 m/s) can cause noise, water hammer, and pipe erosion. Keep velocities within recommended limits for the operating pressure.
- Condensate. Steam pipes must be pitched to drain condensate. Undrained condensate causes water hammer and reduces effective capacity.
- Insulation. All steam pipes should be insulated to minimize heat loss and maintain steam quality at the point of use.