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Critical flux on a submerged membrane bioreactor for nitrification of source separated urine
被引:12
|作者:
Jiang, Jiaxi
[1
]
Phuntsho, Sherub
[1
]
Pathak, Nirenkumar
[1
]
Wang, Qilin
[1
]
Cho, Jaeweon
[2
]
Shon, Ho Kyong
[1
]
机构:
[1] Univ Technol Sydney UTS, Sch Civil & Environm Engn, Ctr Technol Water & Wastewater, Sydney, NSW 2007, Australia
[2] Ulsan Inst Sci & Technol UNIST, Sch Urban & Environm Engn, UNIST Gil 50, Ulsan 689798, South Korea
基金:
新加坡国家研究基金会;
关键词:
Submerged ultrafiltration membrane bioreactor (UF-MBR);
Critical flux;
Critical flux for irreversibility;
Fouling reversibility;
Source separated urine;
Improved flux-step method;
AMMONIA-OXIDIZING BACTERIA;
COMPLETE NUTRIENT RECOVERY;
WASTE-WATER;
FOULING CONTROL;
INHIBITION;
RESILIENCE;
REMOVAL;
NITRITE;
D O I:
10.1016/j.psep.2021.07.039
中图分类号:
X [环境科学、安全科学];
学科分类号:
08 ;
0830 ;
摘要:
Membrane fouling is the biggest challenge in membrane based technology operation. Studies on critical flux mainly focused on membrane bioreactor for municipal wastewater and/or greywater treatment, which can significantly differ from the ultrafiltration membrane bioreactor (UF-MBRs) to treat source separated urine. In this work, the inhibitory factors on nitrifying bacteria activity were investigated for fast acclimation of nitrifying bacteria with high ammonium concentration and optimization of a high-rate partial nitrification MBR. The maximum nitrification rate of 447 +/- 50 mgN L-1 d(-1) was achieved when concentration of ammonia in feed urine is approximately 4006.3 +/- 225.8 mg N L-1 by maintaining desired pH around 6.2 and FA concentrations below 0.5 mgL(-1). Furthermore, for the first time, the impact of different operational and filtration conditions (i.e. aeration intensity, filtration method, imposed flux, intermittent relaxation, biomass concentration) on the reversibility of membrane fouling was carried out for enhancement of membrane flux and fouling mitigation. Fouling mechanisms for minor irreversible fouling observed under sub-critical condition were pore blocking and polarization. To mitigate membrane fouling, the UF module with effective membrane surface area of 0.02 m(2) is recommended to be operated at the aeration intensity of 0.4 m 3 h(-1), intermittent relaxation of 15 min, biomass concentration of 3.5 g L-1. (C) 2021 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
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页码:518 / 526
页数:9
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