Estimate head loss for liquids through straight horizontal pipes. See velocity, friction factor, and pressure. Use exports, graphs, formulas, and examples for better decisions.
This engineering calculator estimates friction head loss, optional minor losses, pressure drop, velocity, Reynolds number, and friction factor for liquid flow through a horizontal pipe.
| Item | Example Value |
|---|---|
| Flow Rate | 0.015 m³/s |
| Pipe Length | 120 m |
| Inside Diameter | 0.10 m |
| Absolute Roughness | 0.045 mm |
| Fluid Density | 998 kg/m³ |
| Dynamic Viscosity | 1.0 cP |
| Total Minor Loss Coefficient | 1.8 |
| Velocity | 1.909859 m/s |
| Reynolds Number | 190,603.96 |
| Friction Factor | 0.018752 |
| Total Head Loss | 4.519566 m |
| Pressure Drop | 44.2332 kPa |
Darcy–Weisbach equation for major loss:
h_f,major = f × (L / D) × (V² / 2g)
Minor loss equation:
h_f,minor = K × (V² / 2g)
Total head loss:
h_f,total = h_f,major + h_f,minor
Pressure drop:
ΔP = ρ × g × h_f,total
Velocity:
V = Q / A, where A = πD² / 4
Reynolds number:
Re = (ρVD) / μ
Friction factor logic:
f = 64 / ReIt uses Darcy–Weisbach for straight-pipe friction and adds optional minor-loss coefficient K. Friction factor comes from laminar flow relations or the Swamee-Jain turbulent approximation, with a smooth blend through transition.
A horizontal pipe has no elevation head change between ends. This tool therefore focuses on friction and optional fitting losses, then converts total head loss into pressure drop.
You can enter m³/s, m³/h, L/s, L/min, or US gpm for flow. Length, diameter, roughness, density, and viscosity also support multiple practical engineering units.
Higher absolute roughness increases relative roughness. In turbulent flow, that usually raises the friction factor and increases both head loss and pressure drop for the same pipe and flow rate.
When Reynolds number is below 2300, the tool treats the flow as laminar and uses f = 64/Re. Transitional flow uses a blended estimate to avoid a sudden jump.
Yes. Add their combined minor loss coefficient as K. The calculator adds K × V²/(2g) to the straight-pipe loss, giving a more complete total head loss estimate.
Head loss rises quickly with flow because velocity increases with flow, and friction loss depends strongly on velocity. Turbulent friction behavior can make the curve even steeper.
This version is best for liquids and nearly incompressible cases. For gases with meaningful density change, dedicated compressible-flow methods usually produce better results.
Important Note: All the Calculators listed in this site are for educational purpose only and we do not guarentee the accuracy of results. Please do consult with other sources as well.