📦 Resource pdf

Pipe Flow Regime Identification Flowchart (ISO 14383)

The Pipe Flow Regime Identification Flowchart (ISO 14383) is an internationally standardized decision-support tool for classifying multiphase flow regimes—such as bubble, slug, churn, annular, and stratified flow—in horizontal, inclined, or vertical pipes carrying gas-liquid mixtures. It uses dimensionless parameters derived from fluid properties, flow rates, and pipe geometry to systematically determine the dominant flow pattern under given operating conditions. The flowchart enables consistent, repeatable regime identification essential for design, simulation, and safety analysis in oil & gas, chemical, and nuclear industries.

📖 Overview

ISO 14383 provides a graphical and procedural methodology rooted in empirical and semi-empirical hydrodynamic research, consolidating decades of experimental data from two-phase flow studies. It defines regime boundaries using key dimensionless groups—including the liquid and gas Froude numbers, Lockhart–Martinelli parameter (X), and viscosity ratio—to account for gravitational, inertial, and interfacial forces governing phase distribution. The flowchart is structured hierarchically: users first classify pipe inclination (vertical, near-vertical, horizontal/inclined), then compute required dimensionless numbers, and follow branching logic to assign one of up to eight defined flow regimes. Its standardization ensures interoperability across engineering software, regulatory assessments, and operational procedures—particularly where pressure drop prediction, erosion risk, or separation efficiency depends critically on accurate regime identification. While primarily intended for steady-state, adiabatic, non-reactive gas-liquid flows, ISO 14383 includes guidance on applicability limits and cautions regarding high-viscosity liquids, foaming systems, or three-phase (gas–oil–water) flows where supplementary models may be needed.

📑 Key Components

1 Inclination-based classification tree
2 Dimensionless parameter calculation module (Fr_L, Fr_G, X, Φ)
3 Regime boundary correlation maps (e.g., Taitel–Dukler extensions)

🎯 Applications

  • Design and sizing of multiphase pipelines in upstream oil & gas
  • Selection of appropriate pressure drop and holdup correlations in process simulators
  • Risk assessment of flow-induced vibration and liquid slugging in subsea tiebacks

📐 Key Formulas

Liquid Froude Number

Fr_L = u_L / √(g·D·ρ_L/ρ_L)

Dimensionless number representing ratio of liquid inertia to gravity forces; u_L is liquid superficial velocity, g is gravitational acceleration, D is pipe internal diameter

Gas Froude Number

Fr_G = u_G / √(g·D·ρ_G/ρ_L)

Dimensionless number representing ratio of gas inertia to gravity-driven liquid forces; u_G is gas superficial velocity, ρ_G and ρ_L are gas and liquid densities

Lockhart–Martinelli Parameter

X = √[(Δp_L / L) / (Δp_G / L)] ≈ √[(f_L·ρ_L·u_L²)/(f_G·ρ_G·u_G²)]

Ratio of single-phase liquid-to-gas pressure gradients; used to characterize relative momentum flux and define regime transitions

🔗 Related Concepts

Two-phase flow modeling Taitel–Dukler flow regime map Multiphase flow metering

📚 References

#multiphase flow #ISO standard #flow regime