Development of a mixed culture-based combined process for simultaneous removal of higher concentrations of phenol and NH4-N from wastewater

• Simultaneous removal of higher concentrations of phenol (99 %) and NH 4 -N (94 %). • Effective treatment of pre-treated coke oven wastewater with 96 % phenol removal. • Developed combined heterotrophic and autotrophic processes involving anammox. • Suitable for treating wastewaters with COD to NH 4 -N ratios ranging from 1.6 to 3.3. This study develops a mixed culture-based combined process in a dual-stage packed media bioreactor integrating nitrifiers and denitrifiers for the simultaneous removal of phenol and NH 4 -N. The bioreactors operated sequentially in down-flow and up-flow modes, respectively, enabling oxic-anoxic and anaerobic-oxic conditions. During 441 days of continuous operation, using synthetic wastewater and with varied COD to NH 4 -N ratios from 1 to 3.33, the process demonstrated remarkable removal efficiencies: up to 99 % for phenol, 94 % for NH 4 -N, and 88 % for total nitrogen (TN). The corresponding rate of elimination (g/L. d) was: phenol 0.446, NH 4 -N 0.423, and TN 0.396, respectively. This was achieved at a 2-day hydraulic retention time, with initial influent concentrations of 900 mg/L for both phenol and NH 4 -N. The application of the developed process for the treatment of pre-treated coke oven wastewater for 64 days demonstrated sustained removal efficiencies to the extent: of phenol (96 %), NH 4 -N (75 %), and TN (67 %). The corresponding rate of elimination (g/L. d) was: phenol 0.312, NH 4 -N 0.518, and TN 0.462, respectively. Batch studies and microbial molecular techniques of biomass drawn from the reactors confirmed the presence of a mixed culture capable of nitrogen removal involving heterotrophic nitrifiers and aerobic denitrifiers, autotrophic nitrifiers and heterotrophic denitrifiers and anammox species. The developed process scheme shows promise for treating phenol-containing industrial effluents effectively with COD to NH 4 -N ratios ranging from 1.6 to 3.3, leveraging the synergetic actions of both autotrophic and heterotrophic microbes. The study supports majorly UN Sustainable Development Goal 6 by advancing water quality and sustainable water use practices through innovative wastewater treatment technologies.

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Publication Details

Journal
Results in Engineering
Published
2025-03-23
DOI
https://doi.org/10.1016/j.rineng.2025.104700
Citations
2
Primary Topic
Wastewater Treatment and Nitrogen Removal
Type
article
Field-Weighted Citation Impact
1.01

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article

Development of a mixed culture-based combined process for simultaneous removal of higher concentrations of phenol and NH4-N from wastewater

Alka Mehta, Sabumon Pothanamkandathil Chacko, G. Anjali
2 citations
Results in Engineering
Wastewater Treatment and Nitrogen Removal
1.01
article

Development of a mixed culture-based combined process for simultaneous removal of higher concentrations of phenol and NH4-N from wastewater

Alka Mehta, Sabumon Pothanamkandathil Chacko, G. Anjali
article en
2 citations

Abstract

• Simultaneous removal of higher concentrations of phenol (99 %) and NH 4 -N (94 %). • Effective treatment of pre-treated coke oven wastewater with 96 % phenol removal. • Developed combined heterotrophic and autotrophic processes involving anammox. • Suitable for treating wastewaters with COD to NH 4 -N ratios ranging from 1.6 to 3.3. This study develops a mixed culture-based combined process in a dual-stage packed media bioreactor integrating nitrifiers and denitrifiers for the simultaneous removal of phenol and NH 4 -N. The bioreactors operated sequentially in down-flow and up-flow modes, respectively, enabling oxic-anoxic and anaerobic-oxic conditions. During 441 days of continuous operation, using synthetic wastewater and with varied COD to NH 4 -N ratios from 1 to 3.33, the process demonstrated remarkable removal efficiencies: up to 99 % for phenol, 94 % for NH 4 -N, and 88 % for total nitrogen (TN). The corresponding rate of elimination (g/L. d) was: phenol 0.446, NH 4 -N 0.423, and TN 0.396, respectively. This was achieved at a 2-day hydraulic retention time, with initial influent concentrations of 900 mg/L for both phenol and NH 4 -N. The application of the developed process for the treatment of pre-treated coke oven wastewater for 64 days demonstrated sustained removal efficiencies to the extent: of phenol (96 %), NH 4 -N (75 %), and TN (67 %). The corresponding rate of elimination (g/L. d) was: phenol 0.312, NH 4 -N 0.518, and TN 0.462, respectively. Batch studies and microbial molecular techniques of biomass drawn from the reactors confirmed the presence of a mixed culture capable of nitrogen removal involving heterotrophic nitrifiers and aerobic denitrifiers, autotrophic nitrifiers and heterotrophic denitrifiers and anammox species. The developed process scheme shows promise for treating phenol-containing industrial effluents effectively with COD to NH 4 -N ratios ranging from 1.6 to 3.3, leveraging the synergetic actions of both autotrophic and heterotrophic microbes. The study supports majorly UN Sustainable Development Goal 6 by advancing water quality and sustainable water use practices through innovative wastewater treatment technologies.

Results in EngineeringVol. 26
Vellore Institute of Technology University (IN)
Department of Science and Technology, Ministry of Science and Technology, India
Clean water and sanitation
Openalex Percentile: Top 28%
Wastewater Treatment and Nitrogen Removal
1.01
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