Input Parameters
Results
Quick Stats
Example Scenarios
| # | Units | Q | ID | Length | Material | Δz | Temp | Fittings | Action |
|---|
Click Use to load values, then Calculate.
Formulas Used
- Cross‑section area: A = π D² / 4
- Velocity: V = Q / A
- Reynolds number: Re = ρ V D / μ
- Darcy‑Weisbach head loss (major): hf = f (L/D) V²/(2g)
- Minor losses: hm = K V²/(2g), K = Σ(count × Ki)
- Total head: ht = hf + hm + Δz
- Pressure loss: ΔP = ρ g ht
- Friction factor:
- Laminar (Re < 2300): f = 64 / Re
- Turbulent (Re ≥ 4000): Swamee‑Jain: f = 0.25 / [log10(ε/(3.7D) + 5.74/Re^0.9)]²
- Transition (2300–4000): linear interpolation between the two regimes
- Hazen‑Williams (water): hHW = 10.67 L Q1.852 / (C1.852 D4.871) (SI units)
Hazen‑Williams is empirical for water at typical temperatures; use Darcy‑Weisbach for general fluids and wide conditions.
How to Use
- Select SI or US units and a calculation mode.
- Enter either flow or velocity, pipe internal diameter, and length.
- Pick material to set roughness; adjust ε or C if needed.
- Set elevation change and counts for typical fittings and valves.
- Set water temperature or override fluid properties manually.
- Click Calculate to view Darcy and Hazen‑Williams results.
- Use Download CSV or Download PDF for reports.
FAQs
Reference: Pipe Roughness & Hazen‑Williams C
| Material | ε (mm) | ε (in) | C (new) | C (aged) |
|---|---|---|---|---|
| PVC | 0.0015 | 0.000059 | 150 | 145 |
| Copper | 0.0015 | 0.000059 | 140 | 135 |
| Commercial Steel | 0.045 | 0.00177 | 120 | 100–110 |
| Ductile Iron | 0.26 | 0.01024 | 130 | 110–120 |
| Concrete | 0.30 | 0.01181 | 100 | 80–95 |
Values are typical; actual roughness and C decrease as pipes age or foul.
Reference: Minor Loss Coefficients (K) — Typical Values
| Component | K (typical) | Notes |
|---|---|---|
| Elbow 90°, long‑radius | 0.5 | Used in calculator defaults |
| Elbow 90°, short‑radius | 1.5 | Higher loss than long‑radius |
| Elbow 45° | 0.35 | Approximate |
| Gate valve, fully open | 0.17 | Used in calculator defaults |
| Globe valve | 10 | High loss |
| Swing check valve | 2 | Depends on size and condition |
| Tee, through‑run | 0.6 | Used in calculator defaults |
| Tee, branch | 1.8 | Used in calculator defaults |
| Ball valve, full‑port | 0.05 | Low loss |
| Butterfly valve | 0.7 | Varies with opening |
| Sudden contraction | 0.5 | Varies; function of area ratio |
| Sudden expansion | 1.0 | Approx.; exact = (1−A₁/A₂)² |
Choose K values from manufacturer data when available for best accuracy.