Analysis of Hydrodynamic Behavior in Pusher Centrifuges: The Integrated Impact of Rotational Speed, Feed Flow Rate, and Mechanical Vibrations on Wedge Wire Screen Performance

Document Type : Original Article

Author
Department of Mechanical Engineering, Technical and Vocational University (TVU), Tehran, Iran
Abstract
Pusher centrifuges are critical for solid-liquid separation in chemical, pharmaceutical, and wastewater treatment industries, yet their hydrodynamic optimization remains challenging due to complex multiphysics interactions. This study employs integrated CFD simulations and experimental validation to quantify the effects of rotational speed (ω=1200-2000 RPM), feed flow rate (Q=8-9 m³/h), and mechanical vibrations (A=0-3 mm) on pressure/velocity distributions. Key findings reveal that ω dominates system behavior, generating a 178% pressure increase (103.4 to 287.3 kPa) and 65% velocity boost (25.06 to 41.40 m/s) from 1200 to 2000 RPM, following ω² scaling. Surprisingly, Q variations cause <0.1% pressure deviation across tested flow rates, while vibrations induce a linear 4.3% Vₘₐₓ reduction (25.06 to 23.97 m/s) at 3 mm amplitude. The numerical model achieves exceptional agreement with experiments (<3.6% error for pressure, <3.2% for velocity), identifying three operational regimes: (1) ω-controlled steady-state profiles, (2) Q-dependent transient flow stability (70s stabilization time), and (3) vibration thresholds (A>1.5mm) causing turbulence-induced efficiency losses. These quantitative insights enable precise balancing of separation performance (1800 RPM optimal), energy efficiency, and mechanical durability in industrial centrifuges.
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Articles in Press, Accepted Manuscript
Available Online from 22 September 2026

  • Receive Date 11 May 2026
  • Revise Date 15 August 2026
  • Accept Date 22 September 2026
  • Publish Date 22 September 2026