As a new approach for large-scale solid waste utilization and carbon sequestration, carbon sequestration backfilling technology requires a clear understanding of slurry pipeline transport characteristics. As an unstable gas-phase component, the influence of CO2 on multiphase flow behavior must be considered. This study establishes a gas–liquid-solid Eulerian model coupled with Population Balance Model (PBM) to characterize CO2 bubble aggregation and reveal how inlet velocity, pipe diameter and residual CO2 content affect slurry flow characteristics. The results show that: (1) Slurry velocity presents an asymmetric distribution (top > bottom), due to multiphase coupling effect- CO2 enrichment at the top forms a gas–liquid lubricating layer to reduce resistance, while gangue particles deposition at the bottom increases resistance; (2) Parameter sensitivity: Increasing inlet velocity increases flow core velocity and pressure drop; Expanding pipe diameter reduces flow core velocity and pressure drop, while intensifying slurry-particle slip; Increasing residual CO2 content reduces pressure drop, slightly inhibits flow core velocity, and exacerbates the flow core offset. This study confirms residual CO2 content, inlet velocity, and pipe diameter as key parameters regulating pipeline transportation performance of carbon sequestration backfill slurry, providing theoretical support for parameter optimization and energy consumption control of slurry transportation system.
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