Predictive Maintenance

Dyehouse High-Temperature Pump Cavitation & NPSH Margin

At 130 °C most of the system pressure is spent keeping the liquor liquid. Two degrees can cost a seal.

Liquor & System Conditions
°C
bar
kg/m³
Suction Side Pump
m
m
m

NPSH Margin

— m

Available less required; negative means cavitation

Cavitation Assessment

Liquor Vapour Pressure
— bar
NPSH Available
— m
Highest Safe Temperature
— °C
Pressure for Zero Margin
— bar
Available as Share of Required
— ×

Vapour pressure is computed for pure water by the Antoine equation, and dyebath liquor is not pure water — dissolved salts raise the boiling point and lower vapour pressure slightly, which is conservative, while any entrained air or solvent does the opposite and is not. Good practice keeps a margin of at least 0.5 to 1 m over NPSH required rather than merely a positive number, because the published requirement is defined at 3% head drop, by which point cavitation damage is already occurring. Friction loss must be taken at the actual flow with a dirty strainer, not a clean one. **Pressurised high-temperature systems are hazardous**: changes to pressure, temperature or pump duty are engineering decisions for a competent person.

Dyehouse High-Temperature Pump Cavitation & NPSH Margin — free, with the formula and a worked example, at Textile School.