Enter flow in gallons per minute, inside diameter in inches, pipe length in feet and a separately selected Hazen–Williams C coefficient. The default C=130 is an assumed scenario, not a manufacturer value for every pipe. Confirm the coefficient and applicability for the actual material, condition and water conditions.
Hazen-Williams applies to water at ordinary temperatures in turbulent flow, not to other liquids. Fittings, valves, elevation changes and pipe aging add loss. Different sources give slightly different C values.
The tool covers straight pipe, and elevation gain lowers pressure by about 0.433 psi per foot.
Pressure loss (psi) from flow rate
| Flow rate | 8 |
|---|---|
| Pipe diameter | 0.75 |
| Pipe length | 50 |
| Roughness coefficient (C) | 130 |
| Pressure loss (psi) | 5.3 |
| Head loss (feet) | 12.2 |
Common error: Choosing a smaller pipe to save cost on a long run. The pressure lost in the pipe can leave too little at the fixture and force a larger pipe anyway.
Pipe Friction & Pressure Loss: formula
Pipe Friction & Pressure Loss: changing Flow rate
| Flow rate | Pressure loss (psi) | Head loss (feet) |
|---|---|---|
| 6 | 3.1 | 7.2 |
| 7 | 4.1 | 9.5 |
| 8 (example) | 5.3 | 12.2 |
| 9 | 6.6 | 15.2 |
| 10 | 8 | 18.5 |
Pipe Friction & Pressure Loss: compare input ranges
| Input | Tested from | To | Pressure loss (psi): low input | Pressure loss (psi): high input | Swing |
|---|---|---|---|---|---|
| Pipe diameter | 0.675 | 0.825 | 8.8 | 3.3 | 5.5 (104%) |
| Flow rate | 7 | 9 | 4.1 | 6.6 | 2.5 (46%) |
| Roughness coefficient (C) | 117 | 143 | 6.4 | 4.4 | 2 (38%) |
| Pipe length | 45 | 55 | 4.8 | 5.8 | 1.1 (20%) |
Pipe Friction & Pressure Loss: individual input comparisons
| Input | Value | Pressure loss (psi) | Head loss (feet) |
|---|---|---|---|
| Flow rate | 6 | 3.1 | 7.2 |
| 7 | 4.1 | 9.5 | |
| 8 | 5.3 | 12.2 | |
| 9 | 6.6 | 15.2 | |
| 10 | 8 | 18.5 | |
| Pipe diameter | 0.6 | 15.7 | 36.2 |
| 0.675 | 8.8 | 20.4 | |
| 0.75 | 5.3 | 12.2 | |
| 0.825 | 3.3 | 7.7 | |
| 0.9 | 2.2 | 5 | |
| Pipe length | 40 | 4.2 | 9.8 |
| 45 | 4.8 | 11 | |
| 50 | 5.3 | 12.2 | |
| 55 | 5.8 | 13.4 | |
| 60 | 6.4 | 14.7 | |
| Roughness coefficient (C) | 104 | 8 | 18.5 |
| 117 | 6.4 | 14.9 | |
| 130 | 5.3 | 12.2 | |
| 143 | 4.4 | 10.2 | |
| 156 | 3.8 | 8.7 |
Pressure loss (psi): Flow rate against Pipe diameter
| Flow rate / Pipe diameter | 0.6 | 0.75 | 0.9 |
|---|---|---|---|
| 6 | 9.2 | 3.1 | 1.3 |
| 7 | 12.3 | 4.1 | 1.7 |
| 8 | 15.7 | 5.3 | 2.2 |
| 9 | 19.5 | 6.6 | 2.7 |
| 10 | 23.7 | 8 | 3.3 |
Pipe Friction & Pressure Loss: values and definitions
| Quantity and definition | Value used |
|---|---|
| Flow rate — Flow rate through the pipe, in gallons per minute. | 8 |
| Pipe diameter — Inside diameter of the pipe, in inches. | 0.75 |
| Pipe length — Total length of the pipe run, in feet. | 50 |
| Roughness coefficient (C) — Enter a selected Hazen–Williams C coefficient. The default 130 is an assumed scenario, not a verified value for every material. | 130 |
| Pressure loss (psi) | 5.3 |
| Head loss (feet) | 12.2 |
Pipe diameter: half and double
| Pipe diameter | Pressure loss (psi) |
|---|---|
| 0.375 | 154.4 |
| 0.75 | 5.3 |
| 1.5 | 0.182 |
Water loses pressure as it moves through a pipe, and the loss rises steeply with flow and falls steeply with diameter. Eight gallons a minute through 50 feet of three-quarter inch pipe loses about 5.3 psi in this model, about 12.2 feet of head. Halving the diameter would multiply the loss by about 29, since it depends on the diameter to the power of about 4.87.
That is why a small pipe on a long run starves the fixture at the end.
Use the roughness coefficient for your pipe material and age, and add the losses from fittings and valves, which the straight-pipe formula leaves out.
See flow at a velocity on the flow rate calculator, the water in the pipe on the pipe volume page, and the effect of elevation on the drain slope and rafter pages. The duct sizing and static pressure calculators handle air, and the pressure converter changes units.
How does diameter enter this model?
With flow, length and C held fixed, the implemented head loss varies inversely with diameter to the power 4.8655. It is not an unconditional comparison between pipes carrying different flows.
Does elevation affect the pressure result?
The displayed result covers friction only. A separate elevation change alters static pressure; do not count that change as straight-pipe friction.