How to Size a Pulsation Dampener: Why Volume Alone Is Not the Right Calculation

Most pulsation dampeners are selected by volume — the engineer picks a 1-litre or 2-litre unit based on pump flow rate and calls it done. The dampener is installed, the system runs, and the pulsation problem is either solved or it isn’t. When it isn’t, the usual response is to upsize the dampener volume. This […]

The Consequences of Running a Mag Drive Pump with Suspended Solids

Magnetic drive centrifugal pumps are specified for hazardous chemical transfer because they seal completely — no shaft penetration, no dynamic seal, no potential leak path. But that sealed containment shell which eliminates the external leak risk creates a different vulnerability inside: a bearing assembly lubricated by the process fluid, running in a zone with virtually […]

Why Specific Gravity Changes the Motor You Need — Not Just the Flow Curve

When engineers select a centrifugal pump for a chemical application, the most common mistake is treating specific gravity as a flow curve correction and stopping there. The flow-head curve of a centrifugal pump does not change with fluid density — it is the same curve whether you are pumping water at SG 1.0 or sulphuric […]

Piston Motor vs. Diaphragm Motor in a Dosatron: Which One Fails First in Hard Water?

Hard water is one of the most common reasons a Dosatron unit starts dosing inconsistently or stops working altogether. The mechanism is straightforward: calcium and magnesium carbonates precipitate out of solution as the water passes through the unit, and the deposits accumulate on the mechanical components that make the dosing motor work. Which motor design […]