The fluid patterns and structure optimization of a novel continued-flow integrated biological
reactor (CIBR) were explored by using the computational fluid dynamics (CFD). The results
of the CFD simulation revealed that both the liquid velocity field and the gas volume fraction
in the CIBR showed an axisymmetric spatial distribution. Furthermore, increasing the aperture sizes
of below diversion holes from 2 cm to 8 cm could significantly enhance the turbulent kinetic energy
of three-phase separation zone. Consequently, the solid-liquid separation and the treatment efficiency
of CIBR were enhanced. In addition, an increase in the angle of the inclined plate (from 35° to 45°
and further to 50°) caused increases in the liquid velocity, volatility and gas holdup in the threephase
separation zone, while decreased gradually in the settling zone. These changes improved gasliquid
separation in the three-phase separation zone and the sludge sedimentation in the settling zone.
The findings of the study provide an insight into the fluid characteristics of gas-liquid-solid three phases
within the CIBR.
CONFLICT OF INTEREST
The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.
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Development of a novel Moving Bed Biofilm Reactor (MBBR) for treatment of wastewaters by improving the hydrodynamics Himanshu Tiwari, Elsa Sony, Rahul Jayakumar, Sivaraman Savithri, Girish R. Pophali Journal of Water Process Engineering
Modeling and Control Strategies for Energy Management in a Wastewater Center: A Review on Aeration Mukhammad Jamaludin, Yao-Chuan Tsai, Hao-Ting Lin, Chi-Yung Huang, Wonjung Choi, Jiang-Gu Chen, Wu-Yang Sean Energies
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