Identifying the Effect of Non-Ideal Mixing on a Pre-Denitrification Activated Sludge System Performance through Model-Based Simulations
Author(s) -
Malek G. Hajaya
Publication year - 2019
Publication title -
jordanian journal of engineering and chemical industries (jjeci)
Language(s) - English
Resource type - Journals
eISSN - 2617-720X
pISSN - 2616-9584
DOI - 10.48103/jjeci232019
Subject(s) - activated sludge , denitrification , mixing (physics) , chemistry , effluent , anoxic waters , volume (thermodynamics) , activated sludge model , complete mixing , biomass (ecology) , kjeldahl method , environmental engineering , nitrogen , nitrate , environmental science , pulp and paper industry , mass transfer , environmental chemistry , sewage treatment , chromatography , thermodynamics , ecology , engineering , organic chemistry , physics , quantum mechanics , biology
Effectiveness of a pre-denitrification activated sludge treatment system is governed by the kinetics of the biologicalreactions, and the hydrodynamic mixing behavior in the reactors. Achieving good mixing conditions within a reactor notonly enhances the transfer of reactants but also ensures homogeneous environmental conditions throughout the vesselwhen required, allowing for an effective usage of the reactor’s total volume, leading to optimized, low-cost operation. Inthis work, a pre-denitrification activated sludge system performance with regards to the biological treatment of organiccarbon and nitrogen was investigated, under two scenarios for non-ideal mixing in the anoxic reactor. The systemperformance is simulated based upon the Activated Sludge Model 1 model’s biological reactions, and combining twonon-ideal mixing two-parameter models: CSTR with bypass and dead volume, and two CSTRs with exchange.Performance discrepancies were then identified in the presence of non-ideal mixing. The system’s performance wasfound to be more susceptible to the presence of a dead volume/bypass scenario compared to the two CSTRs withmaterial exchange scenario. Under non-ideal mixing conditions, effluent concentrations of Total Kjeldahl Nitrogen,organic carbon increased marginally, while effluent concentration of nitrate increased significantly. Similarly, the wastestream concentrations of Total Kjeldahl Nitrogen and organic carbon increased significantly as a result of an increase inthe concentration of the heterotrophic biomass. The outcome of this study provides an insight when troubleshooting theoperation of pre-denitrification activated sludge systems for non-ideal mixing conditions.
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