Relationship Between Head and Flow Rate in Centrifugal Pumps
The head (H) and flow rate (Q) of a centrifugal pump have an interdependent relationship, typically represented by the pump performance curve. Understanding this relationship is crucial for proper pump selection and operation.
1. Basic Head-Flow Relationship
Head (H): The energy imparted to the fluid, expressed in meters (m) or feet (ft) of liquid column.
Flow Rate (Q): The volume of liquid delivered per unit time (m³/h, L/s, GPM).
General Trend:
As flow rate (Q) increases, head (H) decreases (for a fixed impeller speed).
At zero flow (shutoff head), head is maximum.
At maximum flow, head drops to its minimum.
This relationship is plotted as the H-Q curve (pump characteristic curve).
2. Why Does Head Decrease with Flow Rate?
Higher flow rates increase friction losses (in pipes, impeller, volute).
Recirculation & turbulence reduce energy transfer efficiency.
Velocity head conversion becomes less effective at high flows.
3. Pump Performance Curve (H-Q Curve)
A typical centrifugal pump curve shows:
Head (H) vs. Flow Rate (Q) – Declining curve.
Efficiency (η) curve – Peaks at the Best Efficiency Point (BEP).
Power (P) curve – Increases with flow.
Key Points on the Curve:
| Operating Point | Head (H) | Flow (Q) | Efficiency (η) |
|---|---|---|---|
| Shutoff (Q=0) | Maximum | Zero | Zero (no flow) |
| Best Efficiency Point (BEP) | Optimal | Optimal | Highest |
| Runout (Max Flow) | Lowest | Maximum | Low (cavitation risk) |
4. Factors Affecting the H-Q Relationship
A. Impeller Diameter
Larger diameter → Higher head at all flows.
Smaller diameter → Lower head.
B. Pump Speed (N)
Affinity Laws predict changes:
Q1Q2=N1N2,H1H2=(N1N2)2Higher speed (N) increases both Q and H.
C. Fluid Viscosity
Higher viscosity reduces flow and head (shifts curve downward).
D. System Resistance (System Curve)
The actual operating point is where the pump curve intersects the system curve.
Higher system resistance (e.g., longer pipes, more fittings) reduces flow.
5. Practical Implications
Operating far from BEP causes:
Low efficiency → Higher energy costs.
Cavitation (at high flow) or overheating (at low flow).
Variable Speed Drives (VSDs) adjust pump speed to match demand, optimizing efficiency.
6. Example: How to Read a Pump Curve
Select desired flow (Q) (e.g., 100 m³/h).
Find corresponding head (H) (e.g., 50 m).
Check efficiency (η) (e.g., 75%).
Ensure NPSH available > NPSH required (to avoid cavitation).
Conclusion
Head (H) decreases as flow (Q) increases in centrifugal pumps.
The H-Q curve helps select the right pump for a system.
Optimal operation is near the BEP for efficiency and longevity.
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