Calculate water-pipe friction head loss, flow rate, required inside diameter, C-factor or pipe length with Hazen-Williams, unit conversions, disclosed C assumptions, velocity and pressure loss.

Estimate straight-pipe friction for water in a full pressurized pipe.

Empirical estimate for turbulent water flow. Excludes elevation, outlet requirements and fitting/valve losses. C presets are planning assumptions; verify actual pipe condition.

Hazen-Williams Equation

The Hazen-Williams equation is used to estimate friction head loss in a full, pressurized pipe carrying water. It is widely used for pipe sizing, pump checks, fire protection hydraulics, irrigation lines, and water distribution systems because it connects flow rate, pipe diameter, pipe length, and pipe roughness in a simple design equation.

hf = K (L Q1.852) / (C1.852 D4.8704)

In this relationship, hf is head loss, Q is flow rate, C is the Hazen-Williams roughness coefficient, D is inside pipe diameter, L is pipe length, and K depends on the unit system being used.

Common Forms of the Equation

A common SI form is:

hf = 10.67 (L Q1.852) / (C1.852 D4.8704)

Use this form when head loss is in meters, pipe length is in meters, flow rate is in m3/s, and diameter is in meters.

A rounded U.S. customary pressure-loss form is:

Δ Pₚₛᵢ = 4.52 (L Q1.85) / (C1.85 D4.87)

This 4.52 form gives pressure loss in psi, with pipe length in feet, flow in US gpm and inside diameter in inches. It does not give feet of head.

Constants must match both input and output units. This calculator converts inputs to SI and consistently uses 10.67, 1.852 and 4.8704. Select the value to solve for and enter the displayed known quantities.

Variable Meanings

Variable Description Why It Matters
hf Head loss due to pipe friction Represents the energy lost as water moves through the pipe
Q Flow rate Higher flow increases friction loss rapidly
C Hazen-Williams roughness coefficient Higher C means a smoother pipe and lower loss
D Inside pipe diameter Diameter has the strongest effect on head loss
L Pipe length Longer pipe creates proportionally more loss

How the Inputs Affect Head Loss

hf ∝ (Q1.852 L) / (C1.852 D4.8704)
  • Flow rate: increasing flow raises head loss sharply.
  • Length: doubling pipe length doubles head loss.
  • Diameter: even a modest increase in diameter can reduce loss dramatically.
  • Coefficient C: smoother, newer, or lined pipe generally has a higher C value and less friction.

In practice, diameter usually has the biggest design impact. That is why upsizing a pipe can reduce friction loss far more effectively than small adjustments to other variables.

Rearranged Forms for Solving Any One Unknown

Select the desired solve mode. These rearranged forms use the same SI convention, with K = 10.67, n = 1.852 and m = 4.8704:

Q = ((hf Cⁿ Dm) / (K L))1 / n
C = ((K L Qⁿ) / (hf Dm))1 / n
D = ((K L Qⁿ) / (hf Cⁿ))1 / m
L = (hf Cⁿ Dm) / (K Qⁿ)

For Hazen-Williams calculations, n is approximately 1.85 and m is approximately 4.87.

Typical Hazen-Williams C Values

The coefficient C depends on pipe material, lining, age, and condition. Typical planning values are:

Pipe Material / Condition Typical C Range
PVC, CPVC, PE, other smooth plastics 140 to 150
Copper or brass 130 to 140
Cement-lined ductile iron 130 to 145
Steel: material and service dependent 120 for wet-system black steel; new smooth steel may use 140 to 150
Concrete pipe 100 to 140
Older rough cast iron or steel 80 to 120

When in doubt, use a conservative C value. Overestimating C can make friction losses look smaller than they really are.

How to Use This Calculator Correctly

  1. Enter the known values for flow rate, pipe length, pipe diameter, and C value.
  2. Select the solve mode; only its required known inputs are shown. Choose Custom C to enter a site-specific coefficient.
  3. Use the inside diameter of the pipe, not just the nominal trade size.
  4. Choose a C value that matches the actual pipe material and condition.
  5. Include fittings, valves, and bends by adding equivalent length or by checking minor losses separately.

The result is the friction head loss along the pipe run only. If your system contains many fittings, elevation changes, or pressure requirements at the outlet, those must be considered in the full hydraulic design.

Head Loss vs. Pressure Loss

Head loss is often converted into pressure loss for pump and system calculations.

Δ P = ρ g hf

For water in U.S. customary units, a useful shortcut is:

Δ Pₚₛᵢ ≈ (hf) / (2.31)

That means every 2.31 feet of water head is about 1 psi.

Example

Suppose water flows at 500 US gpm through 1,000 ft of pipe with C = 130 and an actual inside diameter of 6 inches. Convert to Q = 0.0315450982 m³/s, L = 304.8 m and D = 0.1524 m, then use the calculator’s SI convention:

hf = 10.67 (304.8 × 0.03154509821.852) / (1301.852 × 0.15244.8704) ≈ 6.2570 m

This is approximately 20.5283 ft of water head and 8.8996 psi across the pipe length, using water density 1,000 kg/m³ and standard gravity. The rounded 4.52 pressure form gives about 8.8683 psi; the small difference comes from the rounded empirical constants and exponents. If the same flow were carried in a larger pipe, the friction loss would drop substantially, which is why diameter selection is so important in water system design.

When Hazen-Williams Is a Good Choice

  • Water distribution and service lines
  • Irrigation systems
  • Fire protection piping
  • Preliminary pipe sizing and pump checks
  • Full pipes carrying water under normal operating conditions

When to Use Caution

  • It is an empirical equation developed for turbulent water flow; do not treat it as a general model for other fluids or laminar flow.
  • It is not the best choice for non-water fluids where viscosity matters.
  • It should not be used for partially full gravity pipes or open-channel flow.
  • It can be less appropriate when temperature, fluid properties, or Reynolds number effects are important.

Common Input Mistakes

  • Using nominal pipe size instead of actual inside diameter
  • Selecting a C value that is too optimistic for old or rough pipe
  • Mixing unit systems with the wrong constant
  • Ignoring fittings and valves in the total friction estimate
  • Assuming the equation includes elevation change when it only estimates friction loss