AutoEngCalc - Engineering Calculators

Control Valve Sizing Calculator

IEC 60534 compliant sizing with Cv calculations and flashing/cavitation analysis

4 Control Valve Sizing Tools

Featured: Liquid Flow Sizing with Cv Calculations

Liquid Flow Sizing

Calculate Cv for liquid flow applications

[Diagram will appear here]
Visual representation based on input parameters

Liquid Flow Results

Required Cv: -
Pressure Drop (ΔP): -
Flow Velocity: -
Reynolds Number: -
Viscosity Correction Factor: -

Typical Valve Cv Values

1" Globe Valve

Cv ≈ 5-15

2" Globe Valve

Cv ≈ 20-50

2" Butterfly Valve

Cv ≈ 50-100

4" Butterfly Valve

Cv ≈ 200-400

Gas Flow Sizing

Calculate Cv for gas flow applications

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Visual representation of gas flow

Gas Flow Results

Required Cv: -
Pressure Ratio (P2/P1): -
Flow Type: -
Expansion Factor (Y): -
Critical Pressure Drop: -

Flow Characteristics

Choked Flow Status

Not choked

For gas flows, critical (choked) flow occurs when the pressure ratio reaches:

P2/P1 ≤ [2/(γ+1)]γ/(γ-1)

Choked flow limits the maximum flow rate through the valve.

Two-Phase Flow Sizing

Calculate Cv for two-phase flow applications

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Visual representation of two-phase flow

Two-Phase Flow Results

Required Cv: -
Omega Parameter (ω): -
Flow Regime: -
Homogeneous Density: -
Pressure Recovery Factor (Km): -

Two-Phase Flow Notes

Two-phase flow calculations are complex and depend on:

  • Flow regime (bubbly, slug, churn, annular)
  • Fluid properties of both phases
  • Mass quality (vapor fraction)
  • Pressure drop across the valve

This calculator uses the Homogeneous Equilibrium Model (HEM) for estimation. For critical applications, consult IEC 60534-8-3 standard.

Cavitation Analysis

Analyze cavitation in liquid flow applications

[Diagram will appear here]
Visual representation of cavitation

Cavitation Analysis Results

Cavitation Index (σ): -
Pressure Recovery Factor (FL): -
Critical Cavitation Index: -
Incipient Cavitation: -
Choking Cavitation: -

Cavitation Severity

No Cavitation σ > 2.5

Cavitation occurs when local pressure drops below vapor pressure, forming vapor bubbles that collapse violently.

Severity levels:

  • Incipient: σ ≈ FL² (bubble formation begins)
  • Constant: σ ≈ 1 (steady bubble formation)
  • Choking: σ ≈ FL (maximum flow reached)

Control Valve Sizing Methodology

IEC 60534 Standard

This calculator follows IEC 60534 standards for control valve sizing, which provides internationally recognized methods for:

  • Liquid flow sizing (IEC 60534-2-1)
  • Gas flow sizing (IEC 60534-2-3)
  • Two-phase flow sizing (IEC 60534-2-4)
  • Cavitation analysis (IEC 60534-8-2)

Valve Flow Coefficient (Cv)

The valve flow coefficient (Cv) is defined as the flow of water at 60°F (15.6°C) in US gallons per minute (gpm) at a pressure drop of 1 psi across the valve.

The basic liquid flow equation is:
Cv = Q × √(SG/ΔP)
Where:

  • Q = Flow rate (gpm)
  • SG = Specific gravity (water = 1)
  • ΔP = Pressure drop (psi)

Cavitation and Flashing

Cavitation occurs when the local pressure drops below the vapor pressure of the liquid, forming vapor bubbles that collapse when pressure recovers. This can cause:

Flashing occurs when the outlet pressure remains below vapor pressure, maintaining the vapor phase downstream.