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Engineering ToolBox > Control Valves and Cavitation

Control valves and cavitation, application ratio and multi stage control valves

When a fluid passes a valve the fluid velocity increases and the pressure drops according the Bernoulli equation.

Cavitation

If the speed through the valve is high enough, the pressure in the liquid may drop to a level where the fluid may start bubble or flash. The pressure recovers sufficiently and the bubbles collapse upon themselves.

control valve cavitation

Cavitation may be noisy but is usually of low intensity and low frequency. This situation is extremely destructive and may wear out the trim and body parts of the valve in short time.

Application Ratio

A common way to characterize potential cavitation conditions is the "applications ratio" (or "the incipient cavitation index") and can be expressed as

AR = pi - po / (pi - pv) (1)

where

AR = Application Ratio

pi = inlet pressure, absolute

po = outlet pressure, absolute

pv = vapor pressure of the fluid, absolute

For application ratios above 1 - the fluid flashes. This is not the same as cavitation, but the closer the ratio is to 1, the higher the potential for cavitation.

Note! With an increasing fluid temperature the possibility for cavitation increases.

Example - Flashing Water

If we know the boiling point and the absolute pressure of a fluid (Steam Table with saturated steam properties) the minimum outlet pressure from a valve to avoid flashing can be calculated.

For an application ratio of one equation (1) can modified to

AR = 1 = pi - po / (pi - pv)

or transformed

po = pv

Using "Steam Table" with saturated steam properties we can conclude that

Note! Flashing is not the same as cavitation. Due to local conditions in a valve cavitation may start on much higher outlet pressures.

Multi Stage Control Valves

Cavitation can be avoided by using more than one control valve or more convenient - a multistage control valve.

control valve cavitation multi stages

As illustrated above the "vena contracta" is much lower for a single stage valve than a multi stage valve. Depending on the pressure drop and the temperature of the fluid its possible to avoid cavitation conditions using more than one stage in a valve.

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