Issue |
E3S Web Conf.
Volume 514, 2024
2024 10th International Conference on Environment and Renewable Energy (ICERE 2024)
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Article Number | 01002 | |
Number of page(s) | 15 | |
Section | Ecological Environment Monitoring and Pollution Control | |
DOI | https://doi.org/10.1051/e3sconf/202451401002 | |
Published online | 11 April 2024 |
Optimization of step-feed anoxic-oxic-membrane bioreactor (AO-MBR) with methanol addition for biological nitrogen removal in wastewater using BioWin and response surface methodology (RSM)
1 School of Graduate Studies, Mapúa University, Manila 1002, Philippines
2 School of Chemical, Biological, and Materials Engineering and Sciences, Mapúa University, Manila 1002, Philippines
3 Department of Environmental Engineering, National Cheng Kung University, Tainan 70101, Taiwan
4 Sustainable Environment Research Laboratory (SERL), National Cheng Kung University, Tainan 70101, Taiwan
* Corresponding author: whang@mail.ncku.edu.tw
The study optimized a step-feed anoxic-oxic membrane bioreactor (AO-MBR) with methanol addition, an existing biological nitrogen removal (BNR) process, to improve total nitrogen (TN) removal and to reduce operating costs. Methanol, utilized as an external carbon source, was costly, which led to examining ways to reduce its usage by adjusting the operational parameters and modifying the configuration. The BioWin’s built-in activated sludge model underwent calibration through biokinetic batch experiments and numerical adjustments of stoichiometric and kinetic parameters to create the BNR process model. Dynamic simulations validated the calibrated model. Using the model, a modified configuration with a 20.8% increase in total anoxic volume was proposed. This increased the anoxic hydraulic retention time, improving the denitrification process. The response surface methodology (RSM) was then used to optimize the operating parameters of the modified configuration for maximum TN removal efficiency and minimum operating cost. The optimized parameters found were 0.5 mg/L dissolved oxygen, 45 days of solid retention time, 0:1 methanol distribution ratio, and 1,794.29 L/d methanol, which all enhanced the denitrification process. This resulted in a 16% increase in TN removal efficiency, a 4.12% decrease in operating costs, and an 8.96% reduction in methanol usage.
© The Authors, published by EDP Sciences, 2024
This is an Open Access article distributed under the terms of the Creative Commons Attribution License 4.0, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.
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