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Improving Wastewater Nitrogen Removal and Reducing Effluent NOx--N by an Oxygen-Limited Process Consisting of a Sequencing Batch Reactor and a Sequencing Batch Biofilm Reactor

  • Mehdi Hajsardar EMAIL logo , Seyed Mehdi Borghei , Amir Hessam Hassani and Afshin Takdastan
Published/Copyright: February 14, 2019
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International Journal of Chemical Reactor Engineering
From the journal International Journal of Chemical Reactor Engineering Volume 17 Issue 7

Abstract

A series of reactors including a sequencing batch reactor (SBR) and a sequencing batch biofilm reactor (SBBR) were used for nitrogen removal. The aim of this study was simultaneous removal of NH4+-N and NOx–-N from synthetic wastewater. In the novel proposed method, the effluent from SBR was sequentially introduced into SBBR, which contained 0.030 m3 biofilm carriers, so the system operated under a paired sequence of aerobic-anoxic conditions. The effects of different carbon sources and aeration conditions were investigated. A low dissolved oxygen (DO) level in the biofilm depth of the fixed-bed process (SBBR) simulated the anoxic phase conditions. Accordingly, a portion of NH4+-N that was not converted to NO3–-N by the SBR process was converted to NO3–-N in the outer layer of the biofilm in the SBBR process. Further, simultaneous nitrification and denitrification (SND) was achieved in the SBBR where NO2–-N was converted to N2 directly, before NO3–-N conversion (partial nitrification). The level of mixed liquid suspended solids (MLSS) was 2740 mg/l at the start of the experiments. The required carbon source (C: N ratio of 4) was provided by adding an internal carbon source (through step feeding) or ethanol. Firstly, as part of the system (SBR and SBBR), SBR operated at a DO level of 1 mg/l while SBBR operated at a DO concentration of 0.3 mg/l during Run-1. During Run-2, the system operated at the low DO concentration of 0.3 mg/l. When the source of carbon was ethanol, the nitrogen removal rate (RN) was higher than the operation with an internal carbon source. When the reactors were operated at the same DO concentration of 0.3 mg/l, 99.1 % of the ammonium was removed. The NO3–-N produced during the aerobic SBR operation of the novel method was removed in SBBR reactor by 8.3 %. The concentrations of NO3--N and NO2–-N in the SBBR effluent were reduced to 2.5 and 5.5 mg/l, respectively. Also, the total nitrogen (TN) removal efficiency was 97.5 % by adding ethanol at the DO level of 0.3 mg/l.

When C:N adjustment was carried out SND efficiency at C:N ratio of 6.5 reached to 99 %. The increasing nitrogen loading rate (NLR) to 0.554 kg N/m3 d decreased SND efficiency to 80.7 %.

Keywords: carbon source; nitrogen removal; SND; wastewater; C:N ratio

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Supplementary Material

The online version of this article offers supplementary material (DOI:https://doi.org/10.1515/ijcre-2018-0147).

Received: 2018-06-12
Revised: 2018-10-23
Accepted: 2019-01-28
Published Online: 2019-02-14

© 2019 Walter de Gruyter GmbH, Berlin/Boston

Articles in the same Issue

  1. Articles
  2. Mars van Krevelen Mechanism for the Selective Partial Oxidation of Ethane
  3. Multi-Objective Optimization of an ABE Fermentation System for Butanol Production as Biofuel
  4. Synthesis of Ethyl Phenol over Modified HZSM-5 Catalyst in a Fixed Bed Reactor
  5. Signal Synthesis Model Reference Adaptive Controller with Genetic Algorithm for a Control of Chemical Tank Reactor
  6. Efficiency of Phosphotungstic Acid Modified Mn-Based Catalysts to Promote Activity and N2 Formation for Selective Catalytic Reduction of NO with Ammonia
  7. Mathematical Modelling and Simulation of a Trickle-Bed Reactor for Hydrotreating of Petroleum Feedstock
  8. Improving Wastewater Nitrogen Removal and Reducing Effluent NOx--N by an Oxygen-Limited Process Consisting of a Sequencing Batch Reactor and a Sequencing Batch Biofilm Reactor
  9. CFD Simulation of the Particle Dispersion Behavior and Mass Transfer–Reaction Kinetics in non-Newton Fluid with High Viscosity
  10. Comparison of Euler-Euler and Euler-Lagrange Approaches for Simulating Gas-Solid Flows in a Multiple-Spouted Bed
  11. Numerical Study of Coal Composition Effects on the Performance of Gasification Through Computational Fluid Dynamic
https://doi.org/10.1515/ijcre-2018-0147
Keywords for this article
carbon source; nitrogen removal; SND; wastewater; C:N ratio

Articles in the same Issue

  1. Articles
  2. Mars van Krevelen Mechanism for the Selective Partial Oxidation of Ethane
  3. Multi-Objective Optimization of an ABE Fermentation System for Butanol Production as Biofuel
  4. Synthesis of Ethyl Phenol over Modified HZSM-5 Catalyst in a Fixed Bed Reactor
  5. Signal Synthesis Model Reference Adaptive Controller with Genetic Algorithm for a Control of Chemical Tank Reactor
  6. Efficiency of Phosphotungstic Acid Modified Mn-Based Catalysts to Promote Activity and N2 Formation for Selective Catalytic Reduction of NO with Ammonia
  7. Mathematical Modelling and Simulation of a Trickle-Bed Reactor for Hydrotreating of Petroleum Feedstock
  8. Improving Wastewater Nitrogen Removal and Reducing Effluent NOx--N by an Oxygen-Limited Process Consisting of a Sequencing Batch Reactor and a Sequencing Batch Biofilm Reactor
  9. CFD Simulation of the Particle Dispersion Behavior and Mass Transfer–Reaction Kinetics in non-Newton Fluid with High Viscosity
  10. Comparison of Euler-Euler and Euler-Lagrange Approaches for Simulating Gas-Solid Flows in a Multiple-Spouted Bed
  11. Numerical Study of Coal Composition Effects on the Performance of Gasification Through Computational Fluid Dynamic
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