Self Priming Pump Troubleshooting Guide
Self-Priming Pump Troubleshooting Guide
If you are experiencing issues with your Self Priming Pump, the below guide can help you diagnose any issues, or speak to one of our Technical Sales Engineers for further assistance:
Problem | Possible Cause | Remedy |
Pump not Priming | Casing is Empty or level of fluid is insufficient | Fill pump with Fluid |
Liquid temperature in casing overheated | Add additional fluid, as liquid has recirculated within pump head for too long | |
Air Ingress | Check all pump seals, shaft clearance, suction pipework for possible air entry points | |
Pressurised Delivery Line | Ensure air can escape from delivery line | |
Low Speed | Ensure pump speed is correct and any inverter settings are correct. Check data against performance curve | |
Impeller worn / broken | Check impeller condition | |
Volute worn | Check volute / casing for wear and that the leading edge (cutwater) is intact. Volute/casing should be replaced with impeller to maintain efficiency | |
Strainer blocked | Check any suction strainers for blockage | |
Suction lift requirements Excessive | Check suction pipework friction losses and vertical lift | |
Suction / Discharge lines blocked | Clear all blockages, check all filters and valves | |
Zero fluid delivery | Pump not primed | See above section |
Backpressure too high | Required pressure is beyond capability of pump. Evaluate system specification & design against supplied pump. | |
Friction losses | Check friction losses of all components | |
Impeller Clogged | Clear impeller and clean | |
Suction / Discharge lines blocked | Clear all blockages, check all filters and valves | |
Flow Rate Insufficient | Air Ingress | Check all pump seals, shaft clearance, suction pipework for possible air entry points. Check inlet tank for vortex formations. |
Impeller worn / broken | Check impeller condition or wear plate. Wear plate replacement may not lead to original pump performance being restored. | |
Suction Line Diameter | Suction line diameter too small, viscosity of fluid higher than expected, level of fluid in inlet tank too low | |
Pump Pressure Insufficient | Liquid viscosity is higher than expected | |
High Absorbed Power | Rotational Speed | Check Rotation speed is in line with design, it could be too high |
Cavitation | Head is too low, or delivery pressure requirements too high | |
Liquid Density | Liquid Density is higher than expected | |
Misalignment | Check alignment of pump, coupling and check coupling rubber | |
Internal Friction | Friction between the pump rotating and non-rotating parts | |
Particles within pump | Check fluid and pump for signs of particle ingress. Check inlet filters are sized correctly | |
Vibration | Pump delivery too low | Check NPSHR is being met. Place pressure gauges on discharge and compound gauges on suction |
Pump or pipework not fixed | Check Pump is correctly fixed to baseplate, and pipework is not loose | |
Check NPSHR meets NPSHA | ||
Particles within pump | Check fluid and pump for signs of particle ingress. Check inlet filters are sized correctly | |
Pump Jams | Mechanical Breakdown | Check shaft, coupling, motor, pulleys belts and gearboxes for damage |
Particles within pump | Check fluid and pump for signs of particle ingress. Check inlet filters are sized correctly | |
Short Bearing Life | Lubrication | Ensure bearings are lubricated in accordance with procedure |
Cavitation | Check NPSHR meets NPSHA | |
Particles within bearings | Replace bearings | |
Bearings Rusty | Replace bearings | |
Mechanical Seal Leakage | Particles within pump | Check fluid and pump for signs of particle ingress. Check inlet filters are sized correctly. |
Cavitation | Check NPSHR meets NPSHA | |
Seal overheats | Low Fluid level in pump. Check system and operating procedure. Fluid is recirculating for too long |