Vertiflo Pump Company

The featured range includes vertical sump, end-suction, self-priming, and horizontal process pumps, along with options for specialized operating duties.

It can suit pits or tanks where a vertical arrangement fits the process and available space. Sump depth, liquid level, solids, and installation access influence the selection.

Provide pit depth, mounting elevation, discharge arrangement, and minimum and maximum liquid levels. Include drawings showing obstructions and available removal space.

Suitability depends on the selected construction and the particles present. Describe solids concentration, size, and hardness so the expected wear and operating speed can be evaluated.

Review liquid temperature, vapor pressure, materials, bearings, and sealing requirements. Startup and shutdown conditions can matter as much as the normal operating point.

Many designs do. Follow the model's filling and startup instructions; self-priming capability does not mean the pump may be started empty or operated dry indefinitely.

Start with required flow and total head, then check the operating point against the pump curve. Horsepower or pipe size alone is not enough to select a pump.

Possible causes include suction restrictions, air entry, worn hydraulic components, incorrect rotation, or changed system resistance. Compare measured flow and pressures with the expected operating point.

Cavitation occurs when local pressure falls low enough for vapor bubbles to form and then collapse. Review suction conditions, liquid temperature, and available inlet head when noise or performance changes appear.

Alignment, bearings, impeller condition, mounting, piping strain, and hydraulic conditions can all contribute. Record when vibration occurs so inspection can address the cause rather than just the symptom.

Dry running, unsuitable seal materials, poor flush conditions, shaft movement, or normal wear can cause leakage. Repeated failures warrant a review of the operating conditions and seal arrangement.

Use the model's instructions and service history to set intervals. Track operating hours, leakage, vibration, lubrication requirements, and performance changes rather than relying on a universal calendar schedule.

Compare inspection findings, parts availability, repair cost, downtime, and current duty requirements. Rebuilding is worth evaluating when the casing and major components remain suitable for the application.

It may help when demand varies and the system allows speed adjustment. Check minimum flow, motor suitability, control needs, and measured energy use before estimating savings.

Contact Process & Power at (901) 362-5500 with your location, equipment identification, and application or service concern. The team can review selection, parts, and service options for your needs.

Include the required duty, fluid or process details, operating conditions, utilities, and installation dimensions. For existing equipment, add nameplate photos, model and serial numbers, and a description of the problem or planned change.