The Effect of Mixing Chamber Configuration and Submersion Depth on Centrifugal Aerator Performance

Centrifugal aerators are a vital piece of equipment in water treatment. To improve the efficiency and economy of their operation, a study of their mixing chamber structure and submergence depth was carried out using a combination of numerical simulations and experiments. A centrifugal aerator dissolved oxygen (DO) test bench was built and the numerical simulation was compared with the experiment, the inlet air flow rate showing only a 2.23% error, which verifies the reliability of the numerical simulation. The results show that the capacity of oxygen dissolved in the aeration tank increases and then decreases as the relative area ratio (ð) of the mixing chamber increases, reaching the best capacity at ð = 8.38. In the case of different submergence coefficients (β), the gas volume fraction increased by 31.29% on average at β = 0.15; the standard oxygen transfer rate (SOTR) increased and then decreased with the increase of β, with an average increase of 56.6%. Moreover, the oxygenation performance of centrifugal aerators was significantly improved by the reasonable submergence depth and the structure of the mixing chamber.

[1]  Hou-lin Liu,et al.  Experimental Study of a Gas-Liquid-Solid Three-Phase Flow in an Aeration Tank Driven by an Inverted Umbrella Aerator , 2022, Processes.

[2]  Huaiyu Cheng,et al.  Numerical prediction of cavitation erosion risk in an axisymmetric nozzle using a multi-scale approach , 2022, Physics of Fluids.

[3]  Huaiyu Cheng,et al.  Euler–Lagrange study of cavitating turbulent flow around a hydrofoil , 2021, Physics of Fluids.

[4]  X. Long,et al.  A review of cavitation in tip-leakage flow and its control , 2021, Journal of Hydrodynamics.

[5]  C. Zhang,et al.  Numerical analysis of the effects of gas-phase properties on the internal characteristics and wear in a centrifugal pump , 2020 .

[6]  Hou-lin Liu,et al.  Experimental Study and Numerical Simulation of Gas–Liquid Two-Phase Flow in Aeration Tank Based on CFD-PBM Coupled Model , 2020, Water.

[7]  P. Sharma,et al.  Study on Oxygenation Performance of Solid Jet Aerator having Circular Opening corresponding to Variable Jet Length and Flow Area , 2020, Journal of Physics: Conference Series.

[8]  Hou-lin Liu,et al.  Study on the internal two-phase flow of the inverted-umbrella aerator , 2019, Advances in Mechanical Engineering.

[9]  Zhiren Wu,et al.  Investigation on Oxygenation Performance and Numerical Simulation of Swirling Aerator , 2019, IOP Conference Series: Earth and Environmental Science.

[10]  A. Goel,et al.  Study on oxygen transfer by solid jet aerator with multiple openings , 2018 .

[11]  R. M. Filho,et al.  Influence of impeller type on hydrodynamics and gas‐liquid mass‐transfer in stirred airlift bioreactor , 2015 .

[12]  Pu Xing,et al.  The Fluid-Structure Interaction Analysis of the Inverted Umbrella Aerator Curved Blade , 2014 .

[13]  Kun Li,et al.  Computational Fluid Dynamics Simulation of Flows in an Oxidation Ditch Driven by a New Surface Aerator. , 2013, Environmental engineering science.

[14]  L. Bhuyar,et al.  Effect of Different Configurations of Mechanical Aerators on Oxygen Transfer and Aeration Efficiency with respect to Power Consumption , 2008 .

[15]  Jyeshtharaj B. Joshi,et al.  Mass-Transfer Characteristics of Surface Aerators and Gas-Inducing Impellers , 2004 .

[16]  C. Boyd,et al.  Comparisons of oxygen ― transfer rates and water-circulating capabilities of emergency aerators for fish ponds , 1984 .

[17]  Koichi Fujie,et al.  Operational characteristic evaluation of liquid-pump type deep shaft aerator , 1979 .

[18]  Martin B ´ ilek,et al.  MODELLING OF SINGLE-PHASE FLOW IN THE STATOR CHANNELS OF SUBMERSIBLE AERATOR , 2014 .

[19]  Weidong Shi,et al.  Design and Experimental Research of Self-Suction Sprinkler Irrigation Jet Pump , 2011 .