Recommended Pipe Flow Velocity by Fluid
CONTENTS
Our Products
Recommended Pipe Flow Velocity by Fluid
The recommended pipe flow velocity depends on the fluid, on the working pressure and on whether the line is a suction or a discharge leg. Sizing the pipe below these bands wastes material; sizing it above them costs pressure and erodes valve seats.
ADVISABLE SPEED (M/sc) TABLE FOR MISCELLANEOUS LIQUIDS, GASES AND AIR THAT PASS THROUGH PIPES
Sizing a pipe correctly starts with the flow speed. Too high a velocity causes pressure loss, noise, vibration and erosion of valve seats; too low a velocity oversizes the line. The table below lists the flow speeds normally recommended for water, oil, steam, air and gas in industrial piping.
| Type of flowing material | Advisable speed (m/sn) |
|---|---|
| WATER | |
| City Sustaining Network | 0.60 – 1.50 |
| General Sustaining Lines | 1.50 – 3.00 |
| Vessel Sustaining | 2.00 – 3.00 |
| Suction and Force Pump and Pipe Sustaining Line | 0.75 – 1.50 |
| Hydraulic Liquids | up to 12 M/sc. |
| OIL (HYDRAULIC LIQUIDS) | |
| Pipe-line flow | 3.00 – 7.50 |
| Suction and Force Pump Line | 0.75 – 1.25 |
| STEAM | |
| To be used in heating | 20.0 – 30.0 |
| For general use | 30.0 – 50.0 |
| High Temperature | 50.0 – 70.0 |
| AIR AND GAS | |
| General Sustainment | 20.0 – 75.0 |
How to Use the Recommended Pipe Flow Velocity Table
Read the fluid in the left-hand column, then take the velocity band next to it as the design target. The recommended pipe flow velocity is not a limit that must never be crossed; it is the range in which pressure loss, noise and erosion stay in balance against the cost of a larger pipe and a larger valve.
Three points decide where inside the band a line should sit:
- Suction lines run slower than discharge lines. On a pump suction the recommended pipe flow velocity is held at the low end of the band, because every extra metre per second costs NPSH and brings cavitation closer.
- Solids and aggressive media pull the figure down. Slurries, condensate and chemically active fluids erode seats, elbows and valve trim, so stay below the recommended pipe flow velocity rather than above it.
- Gases and steam tolerate more. Their density is low, so the same velocity carries far less mass per second — which is why the steam and air bands sit well above the water bands in the table.
Once the velocity is fixed the nominal diameter follows from the flow rate. Mark the recommended pipe flow velocity on the vertical axis of the pipe flow diagram, move across to the DN curve of the line and read the volumetric flow rate below it — the worked example under the table follows exactly that route.
Velocity, Pressure Drop and Water Hammer
Pressure drop rises roughly with the square of the velocity: doubling the flow speed in the same bore costs about four times the head. That is why a long run is usually sized at the lower end of the band even when the pump could push more — the pipe is cheaper than the energy it will consume over twenty years.
The second reason is surge. When a fast-closing valve stops a moving column of liquid, the pressure spike is proportional to the velocity that was stopped, not to the working pressure. On lines fitted with quick-acting ball or butterfly valves, holding to the recommended pipe flow velocity is what keeps that spike inside the pressure class of the pipe, the flanges and the valve itself. Where a surge is unavoidable, the answer is a slower closing time or a relief path, not a smaller diameter.
Viscosity shifts the whole picture. Heavy oils and glycol mixtures behave far worse than water at the same speed, so their recommended pipe flow velocity sits lower in the table; thin, clean liquids sit higher.
Nominal Diameter Is Not the Bore
One detail catches people out when they check the chart by hand: the curves behind the recommended pipe flow velocity table are plotted on the real internal diameter of the pipe, not on the DN number. A DN 125 line in DIN 2448 steel measures roughly 133 mm inside, not 125 mm, and flow area grows with the square of the diameter. That is why the worked example below reads 175 m³/h at 3.5 m/s rather than the 155 m³/h a calculation with D = 125 mm would return — a 13 % gap, enough to undersize a pump.
The relation itself is simply Q = V × π D² / 4, with V the recommended pipe flow velocity in m/s, D the internal diameter in metres and Q the flow rate in m³/s (multiply by 3600 for m³/h). Take D from the pipe standard and wall thickness actually being bought, not from the DN label.
Velocity Through the Valve, Not Only the Pipe
The recommended pipe flow velocity band in the table applies to the pipe. Inside a valve the free area is usually smaller, so the local velocity is higher. A reduced-bore ball valve on a DN 100 line typically opens to about 80 mm, which is 64 % of the pipe area and lifts the speed by roughly a factor of 1.6; a butterfly disc standing in the stream does the same thing at part-open positions.
A line designed at the very top of the recommended pipe flow velocity band therefore has no margin left at the trim, and seat erosion, cavitation and noise appear at the valve long before they appear in the straight pipe. On abrasive or high-velocity duties, either size the line towards the middle of the band or specify a full-bore valve, so that the recommended pipe flow velocity in the pipe is also the velocity through the valve.
Related Capacity Tables
Once the velocity is chosen, the matching capacity table gives the diameter directly: steam pipe capacity in kg/h, compressed air pipe capacity in dm³/s, and the pipe flow diagram for water and other liquids.
Example;
The pipe is adjusted to accord the speed of the liquid flows that go through it, and to fit to the requirements in the horizontal and the vertical pipes, the flow speed has been taken as 3,5 m/sc.
The diameter of the pipe where the flow is conducted is taken to be 125 mm.
In order to find the amount conducted Q= m³ according to this data , V= 3,5 m³ / h is marked on the vertical axis, as it is done with the graph. Moving horizontally, it is intersection with DN 125 is found and going down towards the arrow, a flow rate of Q=175 m³/h, is found.
Reference: Engineering ToolBox — recommended flow velocities in water pipes
