Hazen-Williams Calculator

Friction head loss for water in pressure pipe via the SI Hazen-Williams form: head loss in metres and feet, gradient per 100 m, pressure drop in kPa and psi, and velocity with a validity-band advisory — verified C coefficients for six materials plus custom.


Hazen-Williams empirical equation · published C tables

Pipe & Flow

m
mm
L/s

Use the actual internal bore, not the nominal size. C values are new-pipe figures (verified against published tables); old unlined iron mains roughen toward C = 100 — design long-lived systems with an aged C.

Friction Head Loss (water)

1.459m of head over the run
= 4.79 ft, at C = 150
1.459m / 100 m
Hydraulic gradient
14.31kPa
Pressure drop
2.08psi
Pressure drop (imperial)
1.27m/s
Mean velocity

h_f = 10.67·L·Q^1.852/(C^1.852·D^4.87), water only. Straight-pipe friction — add fittings (as equivalent length) and elevation separately for total pump head.

About Hazen-Williams Calculator — Pipe Friction Head Loss for Water

The Hazen-Williams calculator estimates friction head loss for water flowing in pressure pipe — the everyday equation of waterworks, fire-protection, and irrigation design. Enter the pipe length, internal diameter, and flow, pick the material (or enter a custom C), and the tool evaluates the SI form h_f = 10.67·L·Q^1.852/(C^1.852·D^4.87), reporting head loss, the gradient per 100 m, the equivalent pressure drop, and the mean velocity.

Hazen-Williams trades the physical generality of Darcy-Weisbach for pure convenience: one material coefficient C, no viscosity, no iteration. That works because it is calibrated for water at ordinary temperatures and velocities (roughly 0.3–3 m/s). Higher C means smoother pipe — new PVC runs about 150 while old tuberculated cast iron falls to 100, which alone more than doubles the friction loss for the same flow. For other fluids or extreme conditions, use the Darcy-based Reynolds number and pipe sizing tools instead.

How It Works

  1. Enter the pipe run length and internal diameter — the actual bore, not the nominal size (a 4-inch Schedule 40 steel pipe runs 102.3 mm internally; SDR PVC differs again). The D^4.87 exponent makes head loss brutally sensitive to diameter: 10% less bore is about 59% more friction.
  2. Enter the design flow in litres per second and pick the pipe material. The C values are new-pipe figures verified against published tables, except old unlined cast iron, which represents aged, tuberculated mains — water pipes roughen with decades of service, so designers often use a lower "design C" than the new-pipe value.
  3. The tool computes h_f = 10.67·L·Q^1.852/(C^1.852·D^4.87) with Q in m³/s and D in m, then derives the hydraulic gradient (head per 100 m — the number pipe charts tabulate), the pressure drop (ρg·h_f, in kPa and psi), and the mean velocity Q/A.
  4. Check the velocity against the equation's comfort zone: Hazen-Williams is calibrated near 0.9 m/s and stays credible from roughly 0.3 to 3 m/s in turbulent water flow. Outside that — or for hot water, glycol, oils, or any non-water fluid — switch to Darcy-Weisbach.
  5. Straight-pipe friction only: add fitting (minor) losses and elevation change separately for the total pump head. The pipe & duct sizing tool handles fittings via loss coefficients.

Worked Example

A 100 m run of 100 mm-bore PVC (C = 150) carries 10 L/s (0.01 m³/s). Head loss: h_f = 10.67 × 100 × 0.01^1.852 ÷ (150^1.852 × 0.1^4.87) = 10.67 × 100 × 1.977×10⁻⁴ ÷ (10 718 × 1.349×10⁻⁵) = 1.459 m over the run — a 1.46 m per 100 m gradient, equivalent to 14.31 kPa (2.07 psi). The velocity is 0.01 ÷ (π/4 × 0.1²) = 1.27 m/s, comfortably inside the equation's validity range. Swap the pipe for old unlined cast iron (C = 100) and the same flow loses (150/100)^1.852 = 2.12× as much head — 3.09 m — which is why aging mains quietly eat pump energy.

Formulas

Hazen-Williams head loss (SI form)
h_f = 10.67 × L × Q^1.852 / (C^1.852 × D^4.87)
Derived quantities
gradient = h_f/L × 100; Δp = ρ·g·h_f; v = Q / (π/4 · D²)
C sensitivity
h_f2 / h_f1 = (C1 / C2)^1.852

Standards & References

  • Hazen-Williams empirical head-loss equation, SI form with the 10.67 coefficient, as given in standard hydraulics references (e.g. Lindeburg, Civil Engineering Reference Manual; waterworks and fire-protection practice per AWWA and NFPA 13 hydraulic calculations)
  • C coefficients verified against published tables (Engineers Edge Hazen-Williams coefficient table; CECALC design coefficient tables): PVC 150, copper 140, cement-lined ductile iron (new) 140, concrete 130, galvanized steel 120, old unlined cast iron 100 — values vary with age and condition
  • Validity: water near ordinary temperature, turbulent flow, velocities roughly 0.3–3 m/s; for other fluids use Darcy-Weisbach (Reynolds number & friction factor tool)

Frequently Asked Questions

What is the Hazen-Williams equation used for?

Estimating friction head loss for water in pressure pipes — municipal distribution, fire sprinkler hydraulics (NFPA 13 calculations use it), pump discharge lines, and irrigation mains. Its appeal is simplicity: one material coefficient C and no viscosity term or iteration, unlike Darcy-Weisbach with the Colebrook friction factor. The trade-off is that it is only calibrated for water at ordinary temperatures and velocities.

What C value should I use for my pipe?

New-pipe values from the verified table: PVC and other plastics 150, copper and cement-lined ductile iron 140, concrete 130, galvanized steel 120. The critical judgment call is age: unlined iron and steel mains roughen dramatically over decades — old tuberculated cast iron is commonly modeled at C = 100 or below. Designers of long-lived systems often deliberately design with an aged C rather than the shiny catalog number.

How much does pipe diameter matter?

More than anything else in the equation: head loss scales with D^−4.87. Dropping from a 100 mm to a 90 mm bore at the same flow raises friction by (100/90)^4.87 ≈ 1.67× — and going up one commercial size usually cuts head loss roughly in half. When a pump is marginal, one pipe size is nearly always cheaper than one pump size.

When should I use Darcy-Weisbach instead of Hazen-Williams?

Whenever the fluid is not cold-to-warm water, the flow might be laminar or barely turbulent, or velocities leave the ~0.3–3 m/s band: hot water and glycol loops, oils and chemicals, compressed air, very small or very large bores, and precision work. Darcy-Weisbach with the Colebrook friction factor is dimensionally sound for any Newtonian fluid — that is what this site's Reynolds number & friction factor and pipe & duct sizing tools implement.

Does this calculator include fittings and elevation?

No — h_f here is straight-pipe friction only. Total dynamic head for pump selection adds the static lift (elevation difference), fitting and valve losses (minor losses, commonly via K-coefficients or equivalent lengths), and any pressure requirement at the delivery point. Fire-protection and waterworks practice often adds fittings as equivalent pipe lengths, which you can simply add to L in this tool.

How do I convert the head loss to pump pressure?

Multiply by ρg: each metre of water head is 9.807 kPa (1.422 psi per metre, or 0.433 psi per foot). The calculator does this for you, reporting kPa and psi alongside metres and feet. Note the conversion assumes cold water density (1000 kg/m³) — consistent with Hazen-Williams being a water-only equation.