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Control Valve · Free Calculator

Control Valve Cv Calculator (Liquid)

Size a control valve for liquid service. The calculator finds the required Kv and Cv and checks whether the flow is choked (cavitating or flashing) using the IEC 60534-2-1 method.

IEC 60534-2-1Cv and KvChoked flow checkLiquid service
SG
Flow is not choked at this pressure drop.
Required Cv33.37
Required Kv28.87
Sizing pressure drop3 bar
Choked pressure drop8.075 bar
Liquid critical ratio FF0.9566
Flow conditionNormal
How this result was calculated
  1. ΔP = P1 − P2 = 3 bar
  2. FF = 0.96 − 0.28 × √(Pv ÷ Pc) = 0.9566, ΔPchoked = FL² × (P1 − FF × Pv) = 8.075 bar
  3. Kv = Q × √(SG ÷ ΔP) = 50 × √(1 ÷ 3) = 28.87, Cv = 1.156 × Kv = 33.37
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Liquid Valve Sizing Equations

Kv = Q × √(SG ÷ ΔP)   (Q in m³/h, ΔP in bar)
Cv = 1.156 × Kv
ΔPchoked = FL² × (P1 − FF × Pv), FF = 0.96 − 0.28 × √(Pv ÷ Pc)

FL is the liquid pressure recovery factor of the valve (from the manufacturer), Pv the vapour pressure and Pc the critical pressure of the liquid. If the actual ΔP exceeds ΔPchoked, the flow no longer increases and ΔPchoked is used for sizing. This calculator assumes the valve is the same size as the pipe (Fp = 1).

Worked example

50 m³/h of water at 25 °C, P1 = 10 bar(a), P2 = 7 bar(a), FL = 0.9. ΔP = 3 bar, which is below the choked limit of 8.1 bar. Kv = 50 × √(1 ÷ 3) = 28.9 and Cv = 33.4.

Key insight: choose a valve whose rated Cv puts the normal flow at about 60 to 80 % travel. Use the valve rangeability calculator to check the minimum flow too.
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Frequently Asked Questions

What is the difference between Cv and Kv?

Cv is US gallons per minute of water at 1 psi pressure drop; Kv is m³/h of water at 1 bar drop. Cv = 1.156 × Kv.

What is choked flow in a control valve?

When pressure inside the valve falls to the vapour pressure, bubbles form and the flow stops increasing with more pressure drop. This is choked flow and usually comes with cavitation damage.

Where do I find FL for a valve?

FL is published by the valve manufacturer for each valve type and travel. Typical values are about 0.9 for globe valves and 0.5 to 0.7 for butterfly and ball valves at full opening.

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