ℹ️ About This Calculator
Total Dynamic Head (TDH) is the total resistance a pump must overcome to move fluid through a piping system. It combines static head (elevation difference), friction head (pipe and fitting losses), and pressure head (differential between suction and discharge vessels). TDH directly determines the pump power requirement and motor selection.
For HVAC chilled water systems, the typical TDH range is 15–30m for small systems and 30–60m for large central plant systems. Condenser water systems are typically 20–35m. The system curve (TDH vs. flow) intersects the pump curve at the operating point. Always ensure the pump operates within 70–110% of its BEP (best efficiency point) to avoid excessive vibration and premature wear. IS 9137 governs centrifugal pump testing and rating in India.
📐 TDH and Pump Power Formulas
IS 9137 / HI
TDH = H_static + H_friction + H_velocity + H_pressure H_friction (Darcy-Weisbach): hf = f × (L/D) × (v²/2g) f = Moody friction factor (from Colebrook equation) H_friction (Hazen-Williams for water): hf = 10.67 × L × Q^1.852 / (C^1.852 × D^4.87) Pump Power: P_shaft (kW) = ρ × g × Q × TDH / (1000 × η_pump) P_motor (kW) = P_shaft / η_motor Motor selection: next standard size above P_motor × 1.1
🧮 Worked Example
Example: A chilled water booster pump must deliver 20 L/s (72 m³/hr) to an overhead tank 25 m above the sump, through piping with an estimated friction loss of 8 m and negligible pressure head. TDH = 25 + 8 + 0.5 (velocity head) = 33.5 m. Shaft power = ρ×g×Q×TDH/(1000×η_pump) = 1000×9.81×0.02×33.5/(1000×0.72) ≈ 9.13 kW. With motor efficiency 90%, P_motor = 9.13/0.90 ≈ 10.14 kW. Adding a 10% margin, the next standard size 11 kW motor is selected.
📊 Pump Head & Velocity Reference (IS 9137 / HI)
Total Dynamic Head (TDH) is the sum of the static lift (vertical rise), the friction loss in pipe and fittings, and any residual pressure needed at the outlet. Keeping pipe velocities in the recommended band controls both friction loss and noise, and is the first thing to check when a pump runs hot or noisy.
Recommended Water Velocities
| Pipe duty | Velocity (m/s) | Note |
|---|---|---|
| Pump suction | 0.9 – 1.5 | Low, to protect NPSH |
| Pump delivery | 1.5 – 2.5 | Economic range |
| General distribution | 1.0 – 2.0 | Noise limit ~2.4 m/s |
| Long risers / mains | 1.2 – 2.0 | Watch friction loss |
Pump Power
Shaft power P (kW) = (ρ × g × Q × H) / (1000 × ηpump), where Q is flow in m³/s, H is TDH in metres and η is pump efficiency (0.6–0.8 typical). Divide by motor efficiency and add a 10–15% margin, then round up to the next standard motor rating. Undersizing the margin is the usual cause of a pump that cannot meet duty on a hot day.
Velocities are indicative for cold water; verify against the pipe material's friction data and the pump manufacturer's curve.
❓ Frequently Asked Questions
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