If you've ever heard a pump suddenly sound like it's grinding gravel, it's probably cavitating. Here's what's actually happening, in plain language — no equations required.
The one-sentence version: cavitation is liquid boiling inside a pump because the pressure dropped too low — not because it got hot. When those tiny vapor bubbles collapse violently a moment later, they hammer the impeller and slowly destroy it.
Boiling isn't just about temperature — it's about the relationship between temperature and pressure. Water boils at 212°F at sea-level atmospheric pressure, but on top of a mountain, where air pressure is lower, water boils at a lower temperature. The same idea applies inside a pump: if the local pressure at the impeller eye drops low enough, the liquid can start boiling even at room temperature, because there's no longer enough pressure holding it in liquid form.
As liquid accelerates into the pump's impeller eye, its pressure naturally drops (this is normal fluid behavior — pressure and velocity trade off). If the pressure at the suction was already low to begin with, that natural drop can push it below the liquid's vapor pressure, and tiny vapor bubbles form.
The bubbles form in the low-pressure zone right at the impeller eye, then get carried by the flow into a higher-pressure zone further into the pump. The moment they hit that higher pressure, they collapse — violently, and in a fraction of a millisecond. Each collapse sends a tiny, high-velocity jet of liquid slamming into the nearest solid surface, usually the impeller vanes. One bubble collapsing does nothing. Millions of bubbles collapsing continuously, for hours, days, or months, erodes metal — this is why cavitated impellers develop a distinctive pitted, sponge-like surface.
NPSH (Net Positive Suction Head) is simply the engineering way of quantifying "how much pressure margin do we actually have before this liquid starts boiling at the pump inlet." There are two numbers that matter:
As long as NPSHa stays comfortably above NPSHr — engineers typically want at least a 2-3 ft (or more) safety margin — the pump won't cavitate. If NPSHa drops below NPSHr, even briefly, cavitation begins.
Cavitation is one of the most common pump problems in the field, and one of the easiest to misdiagnose as 'a bad pump' when the real issue is upstream in the piping or installation.
Besides the gravel/rattling noise, watch for: erratic pressure gauge readings that flicker instead of holding steady, reduced flow output compared to the pump curve, excessive vibration, and unexplained bearing or seal failures on an otherwise well-maintained pump. If several of these show up together, suspect cavitation before assuming the pump itself has failed.
In the field, cavitation is usually a suction-side problem, not a pump defect: the pump mounted too high above the liquid source (exceeding its suction lift capability), a clogged suction strainer restricting flow, a suction pipe that's too long or too small in diameter, too many elbows/fittings on the suction side creating friction losses, a partially closed suction valve, or air leaking into the suction line through a bad gasket or fitting.
Before condemning a pump, check: is the suction strainer clean? Is the suction valve fully open? Is the liquid level in the source tank/sump adequate (not close to running dry, which lets air/vapor into the suction)? Has the liquid temperature increased (hotter liquid has less NPSH margin)? Has the pump been moved further from or higher above the source since it last worked correctly? These five checks resolve a large share of field cavitation complaints without replacing the pump.
NPSH (Net Positive Suction Head) is a measure of how much pressure margin exists above a liquid's boiling point at the pump's suction inlet. If that margin runs out, the liquid boils inside the pump even at room temperature — not because it's hot, but because the local pressure has dropped low enough. This boiling is cavitation.
Cavitation happens when the pressure at the pump suction drops below the liquid's vapor pressure, causing tiny vapor bubbles to form. Common causes include the pump being mounted too high above the liquid source, a clogged or undersized suction pipe, a suction line that's too long, a partially closed suction valve, or pumping a hot liquid (hot liquids have higher vapor pressure and less available margin).
Lower the pump relative to the liquid source (increase static suction head), use a shorter and larger-diameter suction pipe to reduce friction losses, avoid unnecessary elbows/valves/fittings on the suction side, keep suction strainers clean, and confirm the pump's required NPSH (NPSHr) is comfortably below the actual available NPSH (NPSHa) — engineers typically target at least a 2-3 ft margin.
Cavitation often sounds like gravel, marbles, or ball bearings rattling around inside the pump casing. This is the audible signature of vapor bubbles collapsing violently against the impeller as they travel into a higher-pressure zone — the same collapse that erodes metal off the impeller over time.
Yes. Repeated cavitation pits and erodes the impeller surface, causes excessive vibration that damages bearings and seals, reduces pump efficiency and flow, and can shorten a pump's service life dramatically. A pump running in cavitation for extended periods can fail in weeks instead of years.