50 L/s

Maximum design flow (180 m³/h)

DN600–DN300

Ductile iron pipeline

1.5 m³

Bladder surge vessel selected

30 s

Minimum closing time for customer demand

The challenge

Cavitation after a pump trip

With all pumps tripping at maximum flow, the unprotected pipeline dropped below the minimum allowed pressure and cavitation occurred. The surge vessel had to be just large enough to prevent this, without exceeding the maximum pressure or draining below its minimum water volume.

Pressure after pump trip without protection
Pressure and pump speed after a trip without protection

Our approach

Transient analysis

  1. WANDA model of the pump station and DN600–DN300 ductile iron pipeline
  2. Pump trip at maximum flow without protection
  3. Parameter study of vessel volume and pre-charge pressure
  4. Selected vessel checked against minimum and maximum pressure and minimum liquid volume
  5. Inadvertent closure of the customer demand with three pumps running
Flow during customer demand closure
Flow during closure of the customer demand

Results

Key results

Key findings

  • Without protection, a pump trip causes sub-atmospheric pressure and cavitation.
  • A vertical bladder surge vessel of 1.5 m³ with a 1.0 m pre-charge meets all criteria.
  • The customer demand should close in no less than 30 s to avoid excessive pressure.
  • The vessel must stay online at all times. A standby vessel is recommended so protection continues during maintenance.

Working on a similar project?

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