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Control Valve Cavitation Index Calculator

The cavitation index (sigma) shows how close a liquid control valve is to cavitating. Compare the service sigma with the choked flow value from the valve’s FL.

Sigma σCavitationFlashingFL factor
σ below about 2: cavitation is likely to start inside the valve. Check the manufacturer’s incipient σ for this trim.
Service σ1.661
Choked flow σ (1/FL²)1.235
Pressure drop ratio0.600
How this result was calculated
  1. σ = (P1 − Pv) ÷ (P1 − P2) = 9.9683 ÷ 6 = 1.661
  2. σchoked ≈ 1 ÷ FL² = 1.235
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Cavitation Index

σ = (P1 − Pv) ÷ (P1 − P2)
σchoked ≈ 1 ÷ FL²

Higher σ means less risk. Manufacturers publish incipient, constant and damaging cavitation σ values for each trim (ISA RP75.23); the 2.0 guide used here is a typical rough threshold.

Worked example

Water at 25 °C from 10 to 4 bar(a): σ = (10 − 0.032) ÷ 6 = 1.66. With FL = 0.9 the choked value is 1.23, so the valve is cavitating but not choked.

Key insight: cavitation damage happens where the bubbles collapse, usually downstream of the vena contracta. Lowering the pressure drop per stage, not just choosing harder materials, is the real cure.
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Frequently Asked Questions

What is a cavitation index?

A ratio comparing the pressure available above vapour pressure with the pressure drop across the valve. Lower values mean more cavitation.

What is the difference between cavitation and flashing?

In cavitation the vapour bubbles collapse as pressure recovers; in flashing the outlet pressure stays below vapour pressure and the liquid leaves partly as vapour.

How can cavitation be prevented?

Reduce the drop per stage with multi stage trims, place the valve where pressure is higher, or use a valve with a higher FL.

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