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
📑 Key Components
🎯 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