Abstract
In water resource recovery facilities (WRRF), aeration efficiency and N2O greenhouse gas emission are affected by the variability of the α-factor. Dynamic calibration of α using sensor data represents a significant knowledge gap this contribution aims to address. To assess factors influencing oxygen and N2O gas mass-transfer, a continuous flow laboratory-scale reactor system was operated to encourage the proliferation of filamentous bacteria. Gas mass-transfer was assessed using fine-bubble and surface aeration. Significant impacts of solid settling velocity on the α-factor – relative to that by MLSS concentration – is obtained. The feasibility of using solid settling velocity and concentration, as α-factor predictors, is tested. The theoretical approach of using relative diffusivity to dissolved oxygen – as an effective predictor of N2O liquid–gas mass-transfer stripping – is experimentally validated, for the first time. Plant-wide WRRF simulations show that surface aeration is inferior to fine-bubble aeration in terms of greenhouse gas emission and treated water quality.
Original language | English |
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Article number | 150650 |
Number of pages | 9 |
Journal | Chemical Engineering Journal |
Volume | 488 |
Early online date | 26 Mar 2024 |
DOIs | |
Publication status | Published - 15 May 2024 |
Data Availability Statement
Data will be made available on request.Keywords
- Alpha-factor modelling
- Filamentous bulking
- Gas mass transfer in activated sludge reactors
- Laboratory-scale experiments
- WRRF simulations
ASJC Scopus subject areas
- General Chemical Engineering
- General Chemistry
- Industrial and Manufacturing Engineering
- Environmental Chemistry