Typical Minor Loss Coefficients (K)
- 90° elbow: ~0.75
- 45° elbow: ~0.40
- Tee (through/run): ~0.60
- Tee (branch): ~1.80
- Ball valve (open): ~0.05
- Check valve: ~2.00
- Union: ~0.08
Rule of thumb: a handful of tight bends can equal several feet of extra head.
Size your pump by required flow and total dynamic head (TDH). Supports US/Metric, turnover or process flow, and plumbing losses.
Use the guidance below to choose a pump that reliably meets your required flow at the computed Total Dynamic Head (TDH).
Inputs: 200 gal fish tank, turnover 1.5×/h → 300 GPH. Media bed: 300 L, fill fraction 0.6, fill in 10 min (sequential) → 18 L/min ≈ 285 L/h ≈ 75 GPH. Required flow is max(300, 75) = 300 GPH. Add 20% margin → 360 GPH.
Head & plumbing: 4 ft vertical, 20 ft of 1″ PVC, 4× 90°, 2× 45°, 1× tee (run), 1× tee (branch), 1× ball valve, 2× unions, extra 0.5 ft for screens. Calculator gives TDH ≈ 7.2 ft (example).
Selection: Choose a pump whose curve at 7.2 ft is ≥ 360 GPH. Verify shutoff head ≥ ~1.25×TDH (≈ 9 ft).
Rule of thumb: a handful of tight bends can equal several feet of extra head.
Lower C → higher friction. If your system clogs, your TDH increases and flow drops.
If between sizes, choose the larger and add a valve to trim flow.
Calculate both and use the higher result, then add your safety margin.
Labels show zero-head flow. Real systems have vertical lift, friction, and minor losses. Always size by the pump curve at your TDH.
Yes. Larger diameter reduces velocity and friction, often recovering hundreds of LPH/GPH at the same head.
15–30% extra flow or shutoff head is typical to cover fouling, seasonal changes, and minor upgrades.