Pipe Flow Theory
Introduction
Pipe flow calculations are fundamental to process engineering, determining the pressure drop and head loss in piping systems. Understanding these principles is essential for pump sizing, system design, and energy optimization.
The primary equation for calculating frictional pressure drop in pipes is the Darcy-Weisbach equation, which relates pressure loss to fluid velocity, pipe dimensions, and the friction factor.
Darcy-Weisbach Equation
The Darcy-Weisbach equation calculates the pressure drop due to friction:
Where:
- ΔP = Pressure drop (Pa)
- f = Darcy friction factor (dimensionless)
- L = Pipe length (m)
- D = Pipe inner diameter (m)
- ρ = Fluid density (kg/m³)
- V = Average flow velocity (m/s)
The head loss form is often more convenient:
Reynolds Number
The Reynolds number determines the flow regime and is essential for friction factor calculation:
Laminar Flow
Re < 2,300
Smooth, orderly flow layers
Transitional
2,300 < Re < 4,000
Unstable, unpredictable
Turbulent Flow
Re > 4,000
Chaotic, mixing flow
Friction Factor
Laminar Flow (Re < 2300)
For laminar flow, the friction factor depends only on Reynolds number:
Turbulent Flow (Re > 4000)
For turbulent flow, the Colebrook-White equation is the most accurate:
This implicit equation requires iterative solution. The Swamee-Jain approximation provides a direct explicit solution accurate to within 1%:
Moody Diagram
The Moody diagram is a graphical representation of the friction factor as a function of Reynolds number and relative roughness (ε/D). Key features include:
- Laminar region - Single line where f = 64/Re
- Transitional region - Shaded area (2300 < Re < 4000)
- Turbulent region - Multiple curves for different roughness values
- Fully rough zone - Friction factor independent of Re at high Reynolds numbers
Tip: The calculator displays your operating point on the Moody diagram, making it easy to visualize the flow regime and verify results.
Pipe Roughness Values
Surface roughness (ε) varies by pipe material and condition:
| Material | Roughness ε (mm) |
|---|---|
| Drawn Tubing (Glass, Copper) | 0.0015 |
| Stainless Steel | 0.015 |
| Commercial Steel | 0.045 |
| Galvanized Iron | 0.15 |
| Cast Iron | 0.26 |
| Concrete | 0.3 - 3.0 |
| Riveted Steel | 0.9 - 9.0 |
Minor Losses (Fittings)
Fittings, valves, and other components cause additional pressure losses calculated using K-factors:
Common K-values:
| Fitting | K |
|---|---|
| 90° Elbow (regular) | 0.75 |
| 90° Elbow (long radius) | 0.45 |
| 45° Elbow | 0.35 |
| Tee (through) | 0.4 |
| Tee (branch) | 1.5 |
| Valve/Component | K |
|---|---|
| Gate Valve (full open) | 0.17 |
| Globe Valve | 6.0 |
| Check Valve (swing) | 2.0 |
| Entrance (sharp) | 0.5 |
| Exit | 1.0 |
Design Guidelines
Recommended Velocities
- • Liquids (general): 1-3 m/s
- • Water (suction): 0.5-1.5 m/s
- • Water (discharge): 1.5-3 m/s
- • Gases: 15-30 m/s
- • Steam: 20-40 m/s
Considerations
- • Higher velocity = smaller pipe but more pressure drop
- • Erosion concern for liquids above 3-4 m/s
- • Noise issues for gases above 30 m/s
- • Pressure drop affects pump/compressor sizing
References
- • Perry's Chemical Engineers' Handbook, 9th Edition
- • Crane Technical Paper No. 410 - Flow of Fluids
- • White, F.M. - Fluid Mechanics, 8th Edition
- • Colebrook, C.F. (1939) - "Turbulent Flow in Pipes"