Units
Inputs

Specific gravity SG = ρ/1000 (water reference).

Typical sizing ΔP: 25–33% of system loss for good control authority.

Water 20°C = 0.023 bar a · Water 80°C = 0.473 · Hexane 20°C = 0.16

Critical pressure of fluid (water = 220.6 bar a) used for Fᶠ calc; defaults to 220 bar.

Result
Required Cᵛ (US)
gpm @ 1 psi
Per ISA S75.01 / IEC 60534-2-1.
Required Kᵛ (metric)
m³/h @ 1 bar
Kᵛ = Cᵛ ÷ 1.156
Choked-flow check
Calculation detail
Formula & Method
Cᵛ = Q · √(SG / ΔP)    [Q in US gpm, ΔP in psi] Kᵛ = Q · √(SG / ΔP)    [Q in m³/h, ΔP in bar] Cᵛ = 1.156 · Kᵛ Fᶠ = 0.96 - 0.28 · √(Pᵛ/P_c) (liquid critical-pressure ratio factor) ΔP_choked = Fᴸ² · (P₁ - Fᶠ · Pᵛ)
What this is: Cv (Imperial) and Kv (metric) are the universal flow-coefficient definitions used by every control-valve manufacturer. They tell you how much flow the valve passes per unit of pressure drop. Pick a valve whose published full-open Cv comfortably exceeds your required Cv at maximum design flow. Sizing rule of thumb:
  • Required Cᵛ should fall between 30% and 80% of the valve's max Cᵛ at min and max flow.
  • Below 30% — valve runs near seat, poor controllability, accelerated wear.
  • Above 80% — no margin to handle upset conditions or future flow increase.
Choked flow: when downstream pressure drops low enough that vapour bubbles form in the vena contracta, additional ΔP does not increase flow. The formula returns the maximum useful ΔP; if your operating ΔP exceeds it you are likely cavitating, which destroys trim. Fᴸ depends on valve style — globes have high recovery (less prone to cavitation), butterflies and ball valves are lower-recovery. Brownfield tip: when a process change pushes flow up 30% on an existing valve, do not just throttle further open. Re-run this calc with the new flow, the actual pressure drop available, and the actual Pᵛ / temperature. Many "noisy" or "shaking" valves on revamped units are simply choking. The fix is a different trim (or the next size down so you regain authority), not more positioner tuning.
⚠ For preliminary sizing only Results are based on nominal ASME dimensions and typical material densities. They do not account for manufacturing tolerances, coatings, supports, flanges, fittings, corrosion allowance, or actual site conditions. All final designs must be verified by a qualified engineer and validated against the applicable code edition. Piping Passion accepts no liability for decisions made using this tool.