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<metadata xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xmlns:dc="http://purl.org/dc/elements/1.1/"><dc:title>A simple multiple flow regime modeling approach of induced flow in external loop airlift reactors</dc:title><dc:creator>Zupan,	Bor	(Avtor)
	</dc:creator><dc:creator>Perpar,	Matjaž	(Avtor)
	</dc:creator><dc:creator>Gregorc,	Jurij	(Avtor)
	</dc:creator><dc:creator>Šarler,	Božidar	(Avtor)
	</dc:creator><dc:subject>airlift reactor</dc:subject><dc:subject>homogeneous flow</dc:subject><dc:subject>separated flow</dc:subject><dc:subject>theoretical model</dc:subject><dc:subject>induced flow</dc:subject><dc:subject>pressure loss</dc:subject><dc:description>Accurate treatment of heat and mass transfer processes inside airlift reactors requires accurate velocity field information. This study presents a novel one-dimensional model forecasting induced liquid flow within an external loop airlift reactor across diverse flow regimes. The approach is grounded on homogeneous flow assumption, augmented by a novel correction term derived through modeling of turbulence-induced pressure losses behind gas structures, employing the separated flow model (Lockhart-Martinelli). The model was assessed by comparing the results with purpose-provided experimental data utilizing air and demineralized water. The gas and liquid superficial velocities ranged from 0.001-0.6 m/s and 0.2–1.1 m/s, respectively. Within ± 10 %, an agreement between the novel model and experimental data was observed for both bubbly, separated, and intermediate flow regimes. A similarly robust agreement was confirmed through comparisons with five published experimental datasets. The distinctive feature of this model is its ability to accommodate multiple flow regimes in a unified manner. It circumvents the necessity for specific regime modeling by introducing a correction term with a complexity marginally surpassing that of the conventional homogeneous flow approach. Beyond its primary application in airlift reactors, the model provides a unified framework for modeling two-phase flow hydrodynamics in thermal applications, particularly in flow boiling and bubble-induced convective heat transfer systems. The model’s simple yet effective structure also allows for integration into higher-fidelity heat transfer simulations, making it valuable for boiling heat transfer studies, enhanced cooling strategies, and industrial multiphase flow applications.</dc:description><dc:date>2025</dc:date><dc:date>2025-04-11 10:46:09</dc:date><dc:type>Članek v reviji</dc:type><dc:identifier>168393</dc:identifier><dc:identifier>UDK: 544.014:621</dc:identifier><dc:identifier>ISSN pri članku: 1873-5606</dc:identifier><dc:identifier>DOI: 10.1016/j.applthermaleng.2025.126410</dc:identifier><dc:identifier>COBISS_ID: 232260867</dc:identifier><dc:language>sl</dc:language></metadata>
