Abstract
BACKGROUND: The paper offers a novel interpretation of microbial mechanisms and evaluates the assets of contact stabilization (CS) using multi-component modelling. A model structure re-defining microbial processes is adopted, where the function of the contact tank was limited to the utilization of soluble substrate fractions and that of the stabilization tank essentially involved endogenous decay and removal of the adsorbed particulate substrate. RESULTS: The model was used to simulate the microbial behaviour and performance of CS in comparison with a conventional activated sludge system (CAS), at an SRT range between 6 and 15 d. The results were confirmed by a stoichiometric description of the process using relevant mass balance relationships, which identified the role of major parameters in system behaviour and performance. A rational process design procedure was proposed based on modelling and process stoichiometry. CONCLUSION: The CS process achieved effective carbon removal with a much smaller footprint and/or aeration volume with respect to CAS, due to its ability to work at significantly higher volumetric organic loadings; its flexibility to be operated at much higher SRT compared with CAS with the same HRT, allowed minimizing sludge production and sustaining a microbial composition also supporting nitrification. However, process stoichiometry reflected that the CS process, despite its significant advantages, should not be considered a suitable candidate for maximizing sludge harvest and energy recovery.
Original language | English |
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Pages (from-to) | 1121-1136 |
Number of pages | 16 |
Journal | Journal of Chemical Technology and Biotechnology |
Volume | 93 |
Issue number | 4 |
DOIs | |
Publication status | Published - Apr 2018 |
Bibliographical note
Publisher Copyright:© 2017 Society of Chemical Industry
Keywords
- activated sludge
- design
- modelling
- process