Parameters
Fluid
Pipe diameter D
100 mm
Pipe length L
50 m
Flow velocity v
2.0 m/s
Roughness ε
0.046 mm
Steel:0.046 / Cast iron:0.26 / PVC:0.0015 mm
Fittings & Valves (K-factor)
Friction Factor Method
—
Reynolds number Re
—
Friction factor f
— kPa
Major loss ΔP_major
— kPa
Minor loss ΔP_minor
— kPa
Total loss ΔP_total
— Pa
Velocity head ρv²/2
— L/min
Flow rate Q
— kW
Pump power (η=0.75)
Moody Diagram (operating point ●)
Pressure Distribution Along Pipe Length
Theory Notes
Darcy-Weisbach Equation:
$$\Delta P_{major} = f \cdot \frac{L}{D} \cdot \frac{\rho v^2}{2}$$
Colebrook-White (turbulent):
$$\frac{1}{\sqrt{f}} = -2\log\!\left(\frac{\varepsilon}{3.7D} + \frac{2.51}{Re\sqrt{f}}\right)$$
Minor Losses (K-factor method):
$$\Delta P_{minor} = \sum K_i \cdot \frac{\rho v^2}{2}$$
Reynolds number: $Re = vD/\nu$ (laminar Re<2300, transitional 2300–4000, turbulent Re>4000)
Engineering tip: Typical design velocities are 2–3 m/s for liquids and 15–25 m/s for gases.
High-viscosity oils often have Re<2300 (laminar), where f = 64/Re (Hagen-Poiseuille) applies.
Colebrook-White iteration uses convergence criterion Δf < 1×10⁻⁸ (max 50 iterations).