Published February 2021 | Version v1
Journal article

Analysis of nitrous oxide emissions from aerobic granular sludge treating high saline municipal wastewater

  • 1. UNSW Water Research Centre, School of Civil and Environmental Engineering, University of New South Wales, Sydney, NSW 2052 (Australia)
  • 2. Future Industries Institute, University of South Australia, Mawson Lakes 5095, South Australia (Australia)
  • 3. South Australian Water Corporation, Adelaide, 5000, South Australia (Australia)
  • 4. School of Natural and Built Environments, University of South Australia, Mawson Lakes 5095, South Australia (Australia)
  • 5. Health and Environment Group, School of the Environment, Flinders University, Bedford Park, 5042, South Australia (Australia)

Description

Highlights: • At 3/d the N2O emission factor from AGS and CAS were similar. • Emissions were higher from AGS at loadings >0.6 kg COD/m3/d when compared to CAS. • Functional nitrifying bacterial groups showed no large changes between AGS and CAS. Conventional activated sludge (CAS)-based wastewater treatment processes have the potential to emit high concentrations of nitrous oxide (N2O) during nitrification and denitrification, which can significantly impact the environmental performance and carbon footprint of wastewater treatment operations. While N2O emissions from CAS have been extensively studied, there is little knowledge of N2O emissions from aerobic granular sludge (AGS) which is now an increasingly popular secondary treatment alternative. The N2O emissions performance of AGS needs to be investigated to ensure that the positive benefits of AGS, such as increased capacity and stable nutrient removal, are not offset by higher emissions. This study quantified N2O emissions from a pilot-scale AGS reactor operated under a range of organic loading rates. A second CAS pilot plant was operated in parallel and under identical loading rates to allow for side-by-side comparison of N2O emissions from floc-based activated sludge. Under low loadings of 3/d the N2O emission factor from AGS and CAS were similar, at around 1.46 ± 0.1% g N2Oemitted/g ammonium loaded. A step increase in the organic loading rate increased N2O emissions from AGS more so than CAS which appeared to be attributed to the reactor feeding strategy that was required for AGS formation. The use of a separate anaerobic feeding phase which was followed by the aeration phase, resulted in extended periods of low dissolved oxygen (DO) concentrations combined with an initial high biomass ammonium loading rate, which favours N2O production and was exacerbated at higher organic loads. Conversely, the combined feeding plus aeration operation (aerobic feed) employed by the CAS system enabled a more even biomass ammonium loading rate and DO supply. This work has shown that while AGS has many operational benefits, the impacts that aeration profile, loading rate and feeding strategy have on N2O emissions must be considered.

Availability note (English)

Available from http://dx.doi.org/10.1016/j.scitotenv.2020.143653

Additional details

Identifiers

DOI
10.1016/j.scitotenv.2020.143653;
PII
S0048969720371849;

Publishing Information

Journal Title
Science of the Total Environment
Journal Volume
756
Journal Page Range
vp.
ISSN
0048-9697
CODEN
STENDL

Optional Information

Copyright
Copyright (c) 2020 Elsevier B.V. All rights reserved.