A chemical processing plant was using a centrifugal pump to transfer water-based process fluid from a storage tank to a production line.
Pump Type: End Suction Centrifugal Pump
Capacity: 100 m³/hr
Head: 40 meters
Motor: 22 kW
Operating Hours: 24/7
After 8 months of operation, the pump started showing:
Reduced flow rate
Excessive vibration
Mechanical seal leakage
Increased power consumption
Frequent bearing failures
Symptom Observation
Low Flow Flow reduced from 100 m³/hr to 70 m³/hr
High Vibration Vibration exceeded ISO limits
Seal Leakage Continuous leakage from mechanical seal
Bearing Failure Bearings failed every 2 months
Noise Pump produced cavitation-like sound
The maintenance team measured the suction pressure and found it was lower than the pump manufacturer's requirement.
Available NPSH (NPSHa) was less than Required NPSH (NPSHr).
Cavitation
When pressure at the impeller eye falls below vapor pressure, vapor bubbles form and collapse violently.
Impeller pitting
Vibration
Noise
Reduced efficiency
Seal and bearing damage
Laser alignment revealed:
Motor and pump shafts were misaligned by 0.8 mm.
Misalignment
Bearing overheating
Coupling wear
Mechanical seal failure
Increased vibration
Suction piping had:
Multiple 90° elbows near pump suction
Reducer installed incorrectly
Poor Suction Piping Design
Turbulent flow
Air pockets
Cavitation
Reduced pump efficiency
Pump curve analysis showed the pump was operating far left of BEP (Best Efficiency Point).
Oversized Pump
Internal recirculation
Excess vibration
Increased temperature
Premature seal failure
Failed bearings showed:
Grease contamination
Water ingress
Improper Lubrication Practice
Bearing overheating
Shaft vibration
Reduced bearing life
Failure Mode Root Cause
Impeller Damage Cavitation
Seal Leakage Misalignment + Cavitation
Bearing Failure Misalignment + Poor Lubrication
High Power Consumption Operating Away from BEP
Low Flow Cavitation + Worn Impeller
Corrective Actions
✔ Increased suction pipe diameter
✔ Reduced suction line restrictions
✔ Raised liquid level in tank
✔ Installed proper eccentric reducer
NPSHa > NPSHr
✔ Laser shaft alignment performed
✔ Alignment tolerance maintained within OEM limits
Vibration reduced by 70%
✔ Straight pipe length of 5D before suction
✔ Removed unnecessary elbows
✔ Installed eccentric reducer flat side on top
Smooth flow into impeller
✔ Installed VFD
✔ Adjusted pump speed
Pump operated between 80–110% of BEP
✔ Correct grease quantity
✔ Periodic lubrication schedule
✔ Bearing housing seals replaced
Bearing life increased from 2 months to over 18 months
Parameter Before After
Flow Rate 70 m³/hr 100 m³/hr
Vibration 9.2 mm/s 2.3 mm/s
Seal Life 3 Months 24 Months
Bearing Life 2 Months 18+ Months
Power Consumption 24 kW 20 kW
Pump Efficiency 58% 78%
Top 10 Reasons for Centrifugal Pump Failure
Cavitation
Dry Running
Operating Away from BEP
Misalignment
Pipe Strain
Bearing Lubrication Failure
Mechanical Seal Failure
Air Entrapment
Corrosion/Erosion
Incorrect Pump Selection
Studies across industries show that more than 60% of centrifugal pump failures are caused by cavitation, misalignment, poor lubrication, and operation away from the Best Efficiency Point (BEP). By ensuring proper pump selection, adequate NPSH, correct alignment, good piping practices, and preventive maintenance, pump reliability can be increased significantly while reducing downtime and maintenance costs.