Free Engineering Tool
Pipe Pressure Drop Calculator
Darcy-Weisbach equation with iterative Colebrook-White friction factor. Supports laminar/turbulent flow, pipe roughness presets, and minor losses from fittings.
Results
Darcy-Weisbach Equation
The fundamental equation for pressure drop due to friction in a pipe:
- f — Darcy friction factor (dimensionless)
- L — pipe length (m)
- D — pipe inner diameter (m)
- ρ — fluid density (kg/m³)
- v — mean flow velocity (m/s)
Colebrook-White Equation (Turbulent Flow)
For turbulent flow (Re > 4000), the friction factor is found iteratively:
This calculator uses the iterative Newton-Raphson method (50 iterations) for accurate results matching the Moody diagram.
Laminar Flow
For Re < 2300 (laminar flow), the friction factor is simply:
Minor Losses
Fittings, valves, elbows, and other components add additional pressure drop expressed via K-factors:
| Fitting | K-factor | Fitting | K-factor |
|---|---|---|---|
| 90° elbow (standard) | 0.9 | 45° elbow | 0.4 |
| Tee (through) | 0.4 | Tee (branch) | 1.8 |
| Gate valve (full open) | 0.15 | Ball valve (full open) | 0.05 |
| Check valve (swing) | 2.5 | Globe valve (full open) | 10 |
| Pipe entrance (sharp) | 0.5 | Pipe exit | 1.0 |
| Sudden expansion | ~1.0 | Sudden contraction | ~0.5 |
Pipe Roughness Values
| Material | Roughness ε (mm) | Notes |
|---|---|---|
| Carbon steel | 0.045 | New commercial pipe |
| Stainless steel | 0.015 | Smooth welded |
| Copper | 0.0015 | Drawn tubing |
| Plastic (PE, PVC) | 0.0015 | Very smooth |
| Cast iron | 0.25 | New; aged can be 1–3 mm |
| Hydraulic hose | 0.005 | Rubber inner liner |
| Concrete | 0.3 – 3.0 | Depends on finish |
Practical Example
Given: Q = 60 L/min, D = 25 mm, L = 10 m, steel pipe (ε = 0.045 mm), oil ν = 32 cSt, ρ = 870 kg/m³
v = 4 × 0.001 / (π × 0.025²) = 2.037 m/s
Re = 2.037 × 0.025 / (32 × 10⁻⁶) = 1,592 → Laminar
f = 64 / 1592 = 0.04020
ΔP = 0.04020 × (10/0.025) × 870 × 2.037² / 2 = 29,045 Pa = 0.290 bar
⚠️ Note: In the transition region (Re 2300–4000) the friction factor is interpolated. Real flow may oscillate between laminar and turbulent. Avoid designing systems to operate in this region.
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