Picking a pump is really about one number: total dynamic head. Get it wrong and the pump either starves the system or burns energy throttling against a needlessly oversized curve. This calculator builds TDH from its three real components.
How it works
TDH is the sum of static head, friction head, and velocity head. Friction uses the Hazen-Williams equation in US units:
hf per 100 ft = 0.2083 × (100 / C)^1.852 × Q^1.852 / d^4.8655
velocity (ft/s) = 0.4085 × Q / d²
velocity head = velocity² / (2 × 32.174)
TDH = static head + friction head + velocity head
Here Q is flow in gpm, d is the inside diameter in inches, and C is the
roughness coefficient (150 for PVC down to 100 for old steel). Fitting losses
are folded in by adding their equivalent length to the pipe length.
Worked example
Moving 20 gpm through 150 ft of 1-inch Schedule 40 PVC (ID approximately 1.049 in, C = 150) with 30 ft of equivalent fittings against a 40 ft static lift:
- Friction head over 180 ft effective length ≈ about 14 ft
- Velocity at 20 gpm in 1.049-in pipe ≈ 7.4 ft/s
- Velocity head ≈ 0.85 ft
- TDH ≈ 40 + 14 + 0.85 ≈ 55 ft (illustrative — actual result depends on precise inputs)
For comparison, moving the same 20 gpm through 1.25-inch PVC (ID ≈ 1.364 in, C = 150) cuts friction loss to roughly 4 ft over the same run, dropping TDH to about 45 ft. That one pipe size change saves around 10 ft of head, which translates directly into a smaller, cheaper, quieter pump.
Pipe material and C-factor selection
Hazen-Williams C represents how smoothly a pipe conveys water. Selecting the right value matters:
| Pipe material | Typical C |
|---|---|
| New PVC / HDPE | 150 |
| Copper or brass | 130–140 |
| New steel | 120 |
| Older steel / cast iron | 100 |
| Very old / tuberculated iron | 80–90 |
Using C = 150 for old steel seriously underestimates friction loss; always base C on the pipe’s actual age and condition.
Velocity limits and their purpose
The velocity warning (flag at 8 ft/s discharge, 5 ft/s suction) protects hardware and comfort. Above 8 ft/s in copper or PVC, erosion-corrosion accelerates at fittings and elbows. Above 5 ft/s on the suction side, the drop in local pressure can cause cavitation: vapor bubbles that implode inside the pump impeller, eroding it rapidly and producing a distinctive rattling sound. The velocity head term is usually small — often under 1 ft — but it becomes meaningful in very high-velocity systems.
Reading the pump curve
TDH alone does not select a pump. You must plot your system curve — TDH at several flows — and find where it intersects the pump’s performance curve. The intersection is the actual operating point. An oversized pump will run to the right of its best efficiency point (BEP), drawing excess current and shortening seal and bearing life. The calculator gives you the design-flow TDH; check nearby flows too so you understand the system’s behavior across its range.