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Steam Flow Rate Pipes

Reference data and engineering information about steam flow rate pipes for fluid mechanics applications.

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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:

ΔP=fLDρv22\Delta P = f \cdot \frac{L}{D} \cdot \frac{\rho v^2}{2}

For sizing purposes, velocity can also be expressed through mass flow:

m˙=ρAv=ρπD24v\dot{m} = \rho \cdot A \cdot v = \rho \cdot \frac{\pi D^2}{4} \cdot v

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

SymbolDescriptionUnit
ΔP\Delta PPressure droppsi
ffDarcy friction factor
LLPipe lengthft
DDInside pipe diameterft or in
ρ\rhoSteam densitylb/ft³
vvFlow velocityft/min
m˙\dot{m}Mass flow ratelb/h
AACross-sectional areaft²

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

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Original source layout/search table
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Source: engineeringtoolbox.com

Steam Flow Rate vs. Pressure Drop - Schedule 40 Pipe

17 rows
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 psi1 psi2 psi2 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)
3.5123.5123.5123.5123.5123.5123.512
3/4911141620242935364342506073
1172126313746546668828193114137
1 1/4364553667896111138140170162200232280
1 1/2567084100120147174210218260246304360430
2108134162194234285336410420510480590710850
2 1/217421525831037846054066068082078095011501370
33183804655506608109601160119014301380167019502400
3 1/2462550670800990121814101700174021002000242029503450
464080095011601410169019802400245030002880346042004900
512001430168021002440300035704250438052505100610075008600
619202300282033503960485057006800700086008400100001190014200
839004800557070008100100001140014300145001770016500205002400029500
1072008800102001260015000182002100026000262003200030000370004270052000
121140013700165001950023400284003300040000410004950048000575006780081000

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.

References