Simultaneous nitrogen and phosphorus removal from domestic wastewater in an aerobic granulation system operated at different anaerobic-aerobic durations

被引:0
|
作者
We, A. C. E. [1 ]
Aris, A. [1 ,2 ]
Zain, N. A. M. [2 ,3 ]
Muda, K. [1 ]
Chen, C. X. [1 ]
Sulaiman, S. [4 ]
机构
[1] Univ Teknol Malaysia, Fac Engn, Sch Civil Engn, Dept Water & Environm Engn, Utm Johor Bahru 81310, Johor, Malaysia
[2] Univ Teknol Malaysia, Ctr Environm Sustainabil & Water Secur, Res Inst Sustainable Environm, Utm Johor Bahru 81310, Johor, Malaysia
[3] Univ Teknol Malaysia, Fac Sci, Dept Biosci, Utm Johor Bahru 81310, Johor, Malaysia
[4] Univ Malaysia Pahang, Fac Civil Engn Technol, Kuantan 26300, Pahang, Malaysia
关键词
EXTRACELLULAR POLYMERIC SUBSTANCES; LONG-TERM STABILITY; EXOPOLYSACCHARIDE PRODUCTION; IRON IONS; SLUDGE; GRANULES; STRENGTH; REACTOR; NITRIFICATION; CALCIUM;
D O I
10.1039/d2ew00224h
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The present work investigated the effects of anaerobic-aerobic durations on simultaneous nitrogen and phosphorus removal for the treatment of domestic wastewater in a sequential batch reactor (SBR). Three different anaerobic-aerobic durations, namely M1 (60 min anaerobic and 105 min aerobic), M2 (90 min anaerobic and 75 min aerobic) and M3 (15 min anaerobic and 150 min aerobic) were examined. In this study, M1 with an anaerobic : aerobic ratio of 0.6 : 1 appeared to be the most optimal anaerobic-aerobic duration to ensure the highest simultaneous nitrification and denitrification (SND) and enhanced biological phosphorus removal (EBPR) efficiency of 53.7 +/- 4.6% and 83.4 +/- 2.3%, respectively. Unsatisfactory SND was observed throughout the study. The poor SND efficiency in this study was mainly caused by ineffective nitrification. The nitrification was adversely affected by the high average chemical oxygen demand/nitrogen (COD/N) ratio of 14 in the influent, and the disproportion in the ratio of ammonia-oxidizing bacteria (AOB) and nitrite-oxidizing bacteria (NOB) in the aerobic granules. The shortening of aerobic duration in M2 caused the lowest SND and EBPR efficiency of 26.1 +/- 0.5% and 34.8 +/- 3.7%, respectively. The nitrification and the uptake of orthophosphate by polyphosphate-accumulating organisms (PAOs) during the aerobic reaction were hampered due to the presence of high free nitrous acid (FNA) concentration. Meanwhile, prolonging the aerobic duration in M3 reduced the denitrification efficiency, possibly due to the formation of smaller anaerobic/anoxic zones within the aerobic granules and insufficient carbon source availability, thus contributing to an SND efficiency of 64.2 +/- 3.7%. Finally, this paper demonstrates the importance of maintaining a proper anaerobic : aerobic ratio in governing the formation of aerobic granules with excellent properties, nutrient-removal abilities and healthy microbial dynamics.
引用
收藏
页码:2342 / 2357
页数:16
相关论文
共 50 条
  • [1] Removal of Ammonium Nitrogen from Petrochemical Wastewater by Anaerobic-Aerobic Process
    Zhao, Qing
    Chen, Xin
    Tong, Ming
    Zhao, Yin
    Zhou, Yanbo
    Lu, Jun
    [J]. ASIAN JOURNAL OF CHEMISTRY, 2013, 25 (17) : 9591 - 9594
  • [2] Microbial population dynamics during sludge granulation in an anaerobic-aerobic biological phosphorus removal system
    Zhang Bin
    Ji Min
    Qiu Zhigang
    Liu Huina
    Wang Jingfeng
    Li Junwen
    [J]. BIORESOURCE TECHNOLOGY, 2011, 102 (03) : 2474 - 2480
  • [3] NITROGEN REMOVAL FROM WASTEWATERS - AEROBIC-ANAEROBIC VERSUS ANAEROBIC-AEROBIC PROCESSES
    BECCARI, M
    MARANI, D
    RAMADORI, R
    [J]. EFFLUENT & WATER TREATMENT JOURNAL, 1979, 19 (02): : 65 - &
  • [4] Simultaneous organic and nitrogen removal from municipal landfill leachate using an anaerobic-aerobic system
    Im, JH
    Woo, HJ
    Choi, MW
    Han, KB
    Kim, CW
    [J]. WATER RESEARCH, 2001, 35 (10) : 2403 - 2410
  • [5] An anoxic/anaerobic/aerobic process for the removal of nitrogen and phosphorus from wastewater
    Zhang, B
    Gao, TY
    [J]. JOURNAL OF ENVIRONMENTAL SCIENCE AND HEALTH PART A-TOXIC/HAZARDOUS SUBSTANCES & ENVIRONMENTAL ENGINEERING, 2000, 35 (10): : 1797 - 1801
  • [6] Nitrogen Removal in a Staged Anaerobic-Aerobic Sludge Digestion System
    Kim, Jongmin
    Novak, John T.
    [J]. WATER ENVIRONMENT RESEARCH, 2017, 89 (01) : 17 - 23
  • [7] Removal of pentachlorophenol from wastewater by combined anaerobic-aerobic treatment
    Bhattacharya, SK
    Yuan, Q
    Jin, PK
    [J]. JOURNAL OF HAZARDOUS MATERIALS, 1996, 49 (2-3) : 143 - 154
  • [8] Sequential anaerobic-aerobic treatment for domestic wastewater - A review
    Kassab, G.
    Halalsheh, M.
    Klapwijk, A.
    Fayyad, M.
    van Lier, J. B.
    [J]. BIORESOURCE TECHNOLOGY, 2010, 101 (10) : 3299 - 3310
  • [9] Optimization of the performance of an integrated anaerobic-aerobic system for domestic wastewater treatment
    Tawfik, A.
    El-Gohary, F.
    Ohashi, A.
    Harada, H.
    [J]. WATER SCIENCE AND TECHNOLOGY, 2008, 58 (01) : 185 - 194
  • [10] Granulation for Coking Wastewater Treatment in a Coupled Anaerobic-Aerobic Reactor
    Dong, Chunjuan
    Lv, Bingnan
    [J]. 2018 4TH INTERNATIONAL CONFERENCE ON ENERGY MATERIALS AND ENVIRONMENT ENGINEERING (ICEMEE 2018), 2018, 38