How to use this calculator
- Enter flow and pipe ID. Use actual inside diameter and the design flow rate.
- Enter length and fittings. Use straight pipe length plus a fitting K allowance.
- Set fluid properties. Use density and viscosity at operating temperature.
- Check velocity and loss. Compare velocity, head loss and pressure drop with the system target.
How it works
Flow and pipe inside diameter set velocity:
v = Q / A
Reynolds number sets the friction-factor method:
Re = rho x v x D / mu
Pressure drop uses Darcy-Weisbach plus fitting losses:
dp = (f x L/D + sumK) x rho x v^2 / 2
Head loss converts pressure drop back into equivalent fluid column height:
head = dp / (rho x g)
Worked example
Verified against the live calculator
For 50 L/min through a 25 mm ID pipe over
30 m, water velocity is about 1.7 m/s. With a
small roughness and sumK = 4, the calculator reports the
Darcy pressure drop and equivalent head loss for an early pump/system
screen.
Frequently asked questions
How do you calculate pipe pressure drop?
The calculator uses Darcy-Weisbach: pressure drop equals friction and fitting losses times dynamic pressure. Flow and pipe ID set velocity, viscosity sets Reynolds number and friction factor, and fittings add minor-loss K values.
Is this for plumbing or hydraulic hose?
This page is aimed at water-like pipe systems: plumbing, hydronic, process and shop piping screens. Hydraulic oil hoses should use the hydraulic hose pressure drop calculator because oil viscosity and hose velocity limits differ.
Why does actual pipe ID matter?
Pressure drop changes strongly with diameter. Nominal pipe size is not enough because schedule, material and fittings change the real inside diameter.
Does this size a pump?
No. It reports pipe pressure drop, head loss and hydraulic power loss. Final pump selection needs a pump curve, system curve, valves, strainers, elevation, NPSH and control requirements.
Method & assumptions
- Uses Darcy-Weisbach with laminar f = 64/Re and Swamee-Jain turbulent friction.
- Requires actual pipe inside diameter and fluid viscosity at operating temperature.
- Does not model pump curves, elevation, NPSH, water hammer, pipe aging, valve position, strainers, heat exchange, erosion/corrosion or code requirements.
- Use hydraulic hose pressure drop, pump flow and HP and steel pipe schedule for adjacent sizing checks.