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Valve Sizing: Cv and Kv Calculation Guide for Industrial Valves

Cv (imperial) and Kv (metric) are the universal measures of valve flow capacity — this guide covers the sizing equations for liquid and gas service, cavitation check, and control valve rangeability.

Valve SizingCvKvFlow CoefficientControl Valves

In This Article

  1. 1.Cv to Kv Conversion
  2. 2.Liquid Flow Sizing — ISA S75.01
  3. 3.Cavitation Check — Critical Pressure Drop
  4. 4.Gas Flow Sizing
  5. 5.Control Valve Rangeability

The flow coefficient Cv (or Kv in metric units) is the single most important parameter in valve sizing — it defines how much flow a valve can pass at a given pressure drop. Selecting a valve with too low a Cv causes excessive pressure drop and limits throughput; too high a Cv results in the valve operating near closed position (poor controllability). Correct Cv sizing is critical for both on/off and control valve applications.

Cv to Kv Conversion

Cv (US gallons per minute at 1 psi ΔP, water at 60°F) and Kv (cubic metres per hour at 1 bar ΔP, water at 16°C) are related by: Kv = 0.865 × Cv and Cv = 1.156 × Kv. Most European manufacturers publish Kv; US and API-standard manufacturers publish Cv.

Liquid Flow Sizing — ISA S75.01

For turbulent (non-cavitating) liquid flow: Cv = Q × √(SG / ΔP), where Q = flow rate in US gpm, SG = specific gravity relative to water at 60°F, ΔP = pressure drop across the valve in psi. Example: water at 500 gpm with ΔP = 25 psi: Cv = 500 × √(1.0 / 25) = 500 × 0.2 = 100. Select a valve with Cv ≥ 100 at the specified opening.

Cavitation Check — Critical Pressure Drop

Cavitation occurs when the fluid pressure drops below its vapour pressure at a valve restriction point, forming vapour bubbles that collapse violently downstream — causing noise, vibration, and erosion damage. Check: if ΔP_actual > ΔP_critical = FL² × (P1 − Ff × Pv), cavitation occurs. FL (liquid pressure recovery factor) is published by the valve manufacturer for each valve type. Butterfly valves and ball valves have high FL (0.8–0.9) making them prone to cavitation at high ΔP; anti-cavitation trim globe valves have lower FL (0.4–0.6) specifically for this service.

Gas Flow Sizing

For compressible gas flow at low ΔP (ΔP < P1/2, non-choked): Cv = Q × √(SG_gas × T1 / (520 × P1 × ΔP)), where Q is flow in SCFH. At choked flow (ΔP > P1/2), increase Cv by 1.4–2× — the maximum flow is limited by sonic velocity and additional Cv does not increase flow. Always check whether choked flow conditions apply in control valve sizing.

Control Valve Rangeability

Rangeability is the ratio of maximum to minimum controllable Cv: equal-percentage trim (standard for most applications) provides rangeability of 50:1; linear trim provides 33:1. A control valve with Cv_max = 100 and equal-percentage trim can control flow down to Cv = 2 (100/50). Always verify that the required minimum flow falls within the controllable range — if not, a smaller valve is needed (split-range or cascade control).

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