Limited ozone solubility hampers gas–liquid mass transfer in ozone-based advanced oxidation processes (AOPs), particularly in continuous flow reactors. Herein, high-resolution computational fluid dynamics simulations were integrated with a multi-objective optimisation framework to investigate the influence of geometric parameters on hydrodynamics, bubble dynamics and energy consumption in a static mixer plug flow reactor. Suboptimal gas inlet configurations induced buoyancy-driven gas holdup and backflow, substantially impairing dispersion and mixing uniformity, as indicated by the relative standard deviation (RSD) of gas-phase and bubble size distributions. Optimised inlet position and diameter promoted early fluid bifurcation and shear-induced bubble breakup, improving micro- and macro-mixing. Twisting elements generated localised velocity peaks and strong pressure gradients, efficiently converting pressure into kinetic energy and yielding radially stratified, symmetrical flows, facilitating gas–liquid contact. The number of mixing elements and downstream zone length governed mixing quality and pressure drop, and inlet parameters critically regulated bubble characteristics. The optimised configuration achieved an RSD of 0.790 and a pressure drop of 6435 Pa, reducing mixing heterogeneity and energy consumption by 13.6% and 18.1%, respectively, and yielding a favourable balance between mixing efficiency and energy use. This study establishes a quantitative structure–flow–performance relationship, providing a foundation for scalable, energy-efficient multi-phase reactor design for ozone-based AOPs, along with practical strategies for process intensification and sustainable water treatment.
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