4.7 Article

Start-up strategies to develop aerobic granular sludge and photogranules in sequential batch reactors

期刊

SCIENCE OF THE TOTAL ENVIRONMENT
卷 828, 期 -, 页码 -

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ELSEVIER
DOI: 10.1016/j.scitotenv.2022.154402

关键词

Nitrification and denitrification; C:N ratios; Simultaneous carbon and nitrogen removal; Granular stability; EPS-producing organisms

资金

  1. National Council for Scientific and Technological Development (CNPq)
  2. Coordination for the Improvement of Higher Education Personnel (CAPES)
  3. Science and Technology Foundation of Pernambuco (FACEPE)
  4. BRK Ambiental
  5. Pernambuco Sanitation Company (COMPESA)
  6. Fibra Ambiental e Engenharia Ltd.
  7. National Institute of Science and Technology in Sustainable Wastewater Treatment Plants (INCT Sustainable WTPs)

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In this study, start-up strategies for developing conventional aerobic granular sludge (AGS) and algal aerobic granular sludge (AAGS) (photogranules) were investigated. The results showed that AAGS had better stability and larger diameter, while AGS had a higher abundance of extracellular polymeric substances producing organisms. Variation in feeding time affected the biomass composition, with a 60-min feeding period resulting in higher nitrogen removal efficiency and more compact granules.
In this study, start-up strategies to develop conventional aerobic granular sludge (AGS) and algal aerobic granular sludge (AAGS) (photogranules), were investigated. The granulation experiment was conducted in four sequencing batch reactors (SBR), of which two were conventional SBRs (RC1, RC2) used as control, and two were photo-SBRs (R1, R2). R1 and RC1 were operated with a 40-min feeding during the reactors' anaerobic cycle period, whereas R2 and RC2 with a 60-min feeding. All the reactors were operated in two phases with a C:N = 4:1 in Phase I and 8:1 in Phase II. In Phase I, AGS in RC1 and RC2 was formed 15 days before the AAGS development in R1 and R2. However, the AAGS generally presented better stability and higher diameter. On the other hand, AGS presented greater abundance of extracellular polymeric substances producing organisms, such as Xanthomonadacea and Rhodocyclaceae. Chemical oxygen demand (COD) and NH4+-N removal efficiencies were similar in all the four reactors of approximately 70% and 60%, respectively. In this phase, despite the good biomass structure, the reactors were not able to completely oxidize the high influent concentration of NH4+-N (100 mg.L-1) and COD (400 mg.L-1). This can be associated to the short time of the aerobic phase and low biomass content. In Phase II in all the reactors, a good increase in COD and NH4+-N removal efficiencies to values above 95% and 93%, respectively, was achieved under a higher C:N ratio of 8 with lower influent concentration of NH4+-N (50 mg.L-1). The 60-min anaerobic feeding period in R2 and RC2 resulted in greater removal efficiency of nitrogen, confirming that small variation on cycle periods can affect the biomass composition; the biomass presented more compact granules and larger diameters under 60 min-feeding when compared with those obtained with 40 min-feeding in Phase I.

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