Pipe Flow

Calc

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:

ΔP = f × (L/D) × (ρV²/2)

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:

hf = f × (L/D) × (V²/2g)

Reynolds Number

The Reynolds number determines the flow regime and is essential for friction factor calculation:

Re = ρVD/μ = VD/ν

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:

f = 64/Re

Turbulent Flow (Re > 4000)

For turbulent flow, the Colebrook-White equation is the most accurate:

1/√f = -2 log₁₀(ε/3.7D + 2.51/Re√f)

This implicit equation requires iterative solution. The Swamee-Jain approximation provides a direct explicit solution accurate to within 1%:

f = 0.25 / [log₁₀(ε/3.7D + 5.74/Re⁰·⁹)]²

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:

MaterialRoughness ε (mm)
Drawn Tubing (Glass, Copper)0.0015
Stainless Steel0.015
Commercial Steel0.045
Galvanized Iron0.15
Cast Iron0.26
Concrete0.3 - 3.0
Riveted Steel0.9 - 9.0

Minor Losses (Fittings)

Fittings, valves, and other components cause additional pressure losses calculated using K-factors:

ΔPfitting = K × (ρV²/2)

Common K-values:

FittingK
90° Elbow (regular)0.75
90° Elbow (long radius)0.45
45° Elbow0.35
Tee (through)0.4
Tee (branch)1.5
Valve/ComponentK
Gate Valve (full open)0.17
Globe Valve6.0
Check Valve (swing)2.0
Entrance (sharp)0.5
Exit1.0

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"