2011
DOI: 10.1016/j.watres.2011.04.007
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Study on two operating conditions of a full-scale oxidation ditch for optimization of energy consumption and effluent quality by using CFD model

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Cited by 65 publications
(41 citation statements)
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“…In more recent work, Yang et al (2011) developed CFD simulations based on a mixture gas-liquid model, which were used to optimize oxygen transfer in a fullscale multichannel oxidation ditch equipped with surface rotors and submerged mixers. Additional transport equations representing oxygen transfer and BOD removal were implemented.…”
Section: Previous Modeling Approachesmentioning
confidence: 99%
“…In more recent work, Yang et al (2011) developed CFD simulations based on a mixture gas-liquid model, which were used to optimize oxygen transfer in a fullscale multichannel oxidation ditch equipped with surface rotors and submerged mixers. Additional transport equations representing oxygen transfer and BOD removal were implemented.…”
Section: Previous Modeling Approachesmentioning
confidence: 99%
“…The robustness of OUR monitoring to estimate K L a has been proved in lab reactors in previous studies [27]. Although the OUR can be calculated by the DO profile in the model case [28] or in a pilot plant [29], in practice the DO slope is sensitive to the uneven spatial distribution velocity in the reactor. Therefore, using standard tests to determine in situ OUR was recommended for OTR estimation instead of using DO profiles along the reactor.…”
Section: Process Monitoring Of Our Do Velocity and Shaft Powermentioning
confidence: 97%
“…In the study, they were applied for flow field simulations with the momentum source term approach, and the simulation results were compared with the experimental data. Lou et al (2005), Fan et al (2010), andYang et al (2011) adopted the standard k -e turbulence model in MRF and the moving mesh approach to simulate the flow in the ditch; since all gained good results, the standard k -e turbulence model was used in the MRF and SM simulation cases. In the simulation, the free surface of the ditch was treated as a flat, rigid lid, so a slip wall was given to the surface of the oxidation ditch.…”
Section: )mentioning
confidence: 99%
“…Fan et al (2010) simulated the 3D solid-liquid two-phase flow field in a laboratory-scale oxidation ditch aerated with surface aerators using the multiple rotating reference frame approach (MRF) and the standard k -e turbulence model. Yang et al (2011) predicted the flow field in a full-scale Carrousel oxidation ditch with the 3D standard k -e turbulence model and a modified moving mesh approach. In previous study, we have proposed a momentum source term approach, only based on dimensions and the rotational velocity of aerators, to calculate the flow field in a fullscale Carrousel oxidation ditch ( Jiang et al, 2010).…”
Section: Introductionmentioning
confidence: 99%