Affiliations 

  • 1 Sustainable Process Engineering Centre, Department of Chemical Engineering, Faculty of Engineering, Universiti Malaya, 50603, Kuala Lumpur, Malaysia. Electronic address: loijx@um.edu.my
  • 2 Regional Environment Conservation Division, National Institute for Environmental Studies, Tsukuba, 305-8506, Japan; Research Centre of Water Environment Technology, School of Engineering, The University of Tokyo, Tokyo, 113-8656, Japan. Electronic address: stubo@nies.go.jp
  • 3 Sustainable Process Engineering Centre, Department of Chemical Engineering, Faculty of Engineering, Universiti Malaya, 50603, Kuala Lumpur, Malaysia. Electronic address: fairus.rabuni@um.edu.my
  • 4 Department of Civil Engineering, National Institute of Technology, Wakayama College, Gobo, Wakayama, 644-0023, Japan. Electronic address: takemura@wakayama-nct.ac.jp
  • 5 Regional Environment Conservation Division, National Institute for Environmental Studies, Tsukuba, 305-8506, Japan. Electronic address: aoki.masataka@nies.go.jp
  • 6 Sustainable Process Engineering Centre, Department of Chemical Engineering, Faculty of Engineering, Universiti Malaya, 50603, Kuala Lumpur, Malaysia. Electronic address: adeline@um.edu.my
Chemosphere, 2024 Apr 26;358:142156.
PMID: 38679172 DOI: 10.1016/j.chemosphere.2024.142156

Abstract

Water outages caused by elevated ammonium (NH4+-N) levels are a prevalent problem faced by conventional raw water treatment plants in developing countries. A treatment solution requires a short hydraulic retention time (HRT) to overcome nitrification rate limitation in oligotrophic conditions. In this study, the performance of polluted raw water treatment using a green downflow sponge biofilm (DSB) technology was evaluated. We operated two DSB reactors, DSB-1 and DSB-2 under different NH4+-N concentration ranges (DSB-1: 3.2-5.0 mg L-1; DSB-2: 1.7-2.6 mg L-1) over 360 days and monitored their performance under short HRT (60 min, 30 min, 20 min, and 15 min). The experimental results revealed vertical segregation of organic removal in the upper reactor depths and nitrification in the lower depths. Under the shortest HRT of 15 min, both DSB reactors achieved stable NH4+-N and chemical oxygen demand removal (≥95%) and produced minimal effluent nitrite (NO2--N). DSB system could facilitate complete NH4+-N oxidation to nitrate (NO3--N) without external aeration energy requirement. The 16S rRNA sequencing data revealed that nitrifying bacteria Nitrosomonas and Nitrospira in the reactor were stratified. Putative comammox bacteria with high ammonia affinity was successfully enriched in DSB-2 operating at a lower NH4+-N loading rate, which is advantageous in oligotrophic treatment. This study suggests that a high hydraulic rate DSB system with efficient ammonia removal could incorporate ammonia treatment capability into polluted raw water treatment process and ensure safe water supply in many developing countries.

* Title and MeSH Headings from MEDLINE®/PubMed®, a database of the U.S. National Library of Medicine.

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