<?xml version="1.0" encoding="UTF-8"?><xml><records><record><source-app name="Biblio" version="7.x">Drupal-Biblio</source-app><ref-type>17</ref-type><contributors><authors><author><style face="normal" font="default" size="100%">Salunkhe, Neha Sudhakar</style></author><author><style face="normal" font="default" size="100%">Dastane, Gaurav</style></author><author><style face="normal" font="default" size="100%">Mali, Chaitanya R.</style></author></authors></contributors><titles><title><style face="normal" font="default" size="100%">Coupled computational fluid dynamics-population balance model approach for investigating effect of breakage, coalescence, and interfacial forces in continuous emulsification using static mixers</style></title><secondary-title><style face="normal" font="default" size="100%">Industrial &amp; Engineering Chemistry Research</style></secondary-title></titles><dates><year><style  face="normal" font="default" size="100%">2026</style></year><pub-dates><date><style  face="normal" font="default" size="100%">JAN</style></date></pub-dates></dates><volume><style face="normal" font="default" size="100%">65</style></volume><pages><style face="normal" font="default" size="100%">978-1000</style></pages><language><style face="normal" font="default" size="100%">eng</style></language><abstract><style face="normal" font="default" size="100%">&lt;p&gt;
	This study employs a coupled CFD-PBM framework to investigate the effects of breakage and coalescence kernels as well as interfacial force models on droplet dynamics in turbulent liquid-liquid dispersions. An Euler-Euler two-phase model integrated with the population balance model was used to evaluate the influence of turbulence models and breakup-coalescence kernels on droplet formation. The role of interfacial forces, including drag, lift, and turbulent dispersion, was systematically assessed with respect to interfacial area concentration, dispersed phase volume fraction variation, turbulent dissipation rate, Sauter mean diameter (d 32), and droplet size distribution. Through sensitivity analysis, an optimized CFD-PBM model was developed, capable of accurately predicting droplet dynamics. The predicted d 32 showed excellent agreement with the measured experimental data, with a deviation of approximately 0.2% relative to the reported values. Incorporating the lift force improved the prediction of dispersed phase volume fraction by approximately 6.06%, while the inclusion of the turbulent dispersion force enhanced the phase redistribution and increased the local turbulent dissipation rate in the initial mixing zone by nearly 4.68%, thereby promoting droplet breakage. Furthermore, spectral analysis of velocity time-series data using the fast Fourier transform revealed a -5/3 slope in the energy spectrum, confirming that the simulations captured the inertial subrange of turbulence.&lt;/p&gt;
</style></abstract><issue><style face="normal" font="default" size="100%">1</style></issue><work-type><style face="normal" font="default" size="100%">Article</style></work-type><custom3><style face="normal" font="default" size="100%">&lt;p&gt;
	Foreign&lt;/p&gt;
</style></custom3><custom4><style face="normal" font="default" size="100%">&lt;p&gt;
	4.0&lt;/p&gt;
</style></custom4></record><record><source-app name="Biblio" version="7.x">Drupal-Biblio</source-app><ref-type>17</ref-type><contributors><authors><author><style face="normal" font="default" size="100%">Inamdar, Madhura</style></author><author><style face="normal" font="default" size="100%">Dastane, Gaurav</style></author></authors></contributors><titles><title><style face="normal" font="default" size="100%">Flow-field effects on gas removal and electrolyte distribution in water electrolyzers: a CFD study</style></title><secondary-title><style face="normal" font="default" size="100%">Industrial &amp; Engineering Chemistry Research</style></secondary-title></titles><dates><year><style  face="normal" font="default" size="100%">2026</style></year><pub-dates><date><style  face="normal" font="default" size="100%">JUL </style></date></pub-dates></dates><volume><style face="normal" font="default" size="100%">65</style></volume><pages><style face="normal" font="default" size="100%">15793-15806</style></pages><language><style face="normal" font="default" size="100%">eng</style></language><abstract><style face="normal" font="default" size="100%">&lt;p&gt;
	This study aims to provide a simplified 3D modeling approach for two-phase flow in electrolyzers. Low-temperature electrolyzers operating at high current density exhibit inefficient gas bubble removal, leading to mass-transfer resistance for the electrolyte. To outline an effective gas-removal mechanism, studying two-phase flow dynamics in the porous transport layer (PTL) and flow channels through CFD modeling is essential. Subsequently, a few common flow field designs (serpentine, straight parallel, and inclined parallel) are compared for the two-phase flow dynamics. A modified flow field design is proposed, which allows electrolyte redistribution in the x, y, and z directions and better electrolyte penetration in the PTL. The developed model provides insight into flow and phase interactions along the flow path, aiding in the efficient design of flow fields. The study concludes that the proposed flow field design offers advantages over the conventional design, including greater electrolyte interaction with the PTL and improved gas removal.&lt;/p&gt;
</style></abstract><issue><style face="normal" font="default" size="100%">29</style></issue><work-type><style face="normal" font="default" size="100%">Article</style></work-type><custom3><style face="normal" font="default" size="100%">&lt;p&gt;
	Foreign&lt;/p&gt;
</style></custom3><custom4><style face="normal" font="default" size="100%">&lt;p&gt;
	3.9&lt;/p&gt;
</style></custom4></record></records></xml>