Two moving bed biofilm reactors in series for carbon, nitrogen, and phosphorous removal from high organic wastewaters

被引:16
|
作者
Tsitouras, Alexandra [1 ]
Al-Ghussain, Nour [2 ]
Delatolla, Robert [1 ]
机构
[1] Univ Ottawa, Dept Civil Engn, 161 Louis Pasteur, Ottawa, ON K1N 6N5, Canada
[2] Carleton Univ, Dept Civil & Environm Engn, 1125 Colonel Dr, Ottawa, ON K1S 5B6, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Sequencing batch moving bed biofilm reactor; Cheese production wastewater; Partial nitritation; Enhanced biological phosphorous removal; DAIRY WASTE-WATER; BIOLOGICAL PHOSPHORUS; HETEROTROPHIC NITRIFICATION; CHEESE WHEY; AEROBIC DENITRIFICATION; ACTIVATED-SLUDGE; TREATMENT-PLANT; START-UP; MBBR; PRETREATMENT;
D O I
10.1016/j.jwpe.2021.102088
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Government regulations require on-site treatment of industrial wastewater prior to sewage discharge to prevent environmental degradation of receiving waterbodies. The sequencing batch moving bed biofilm reactor (SBMBBR) can permit on-site treatment of high organic and nutrient content of cheese production wastewater. However, the critical challenge exists of maintaining both an active heterotrophic and an autotrophic population in a single biofilm system treating carbon and ammonia to low discharge levels from cheese production wastewater. Two SB-MBBRs in series separate the heterotrophic and autotrophic communities, circumventing the competition between the heterotrophic and autotrophic populations in a single biofilm system treating wastewater with high carbon to nitrogen ratios. The first reactor (AN/AE) was operated by cycling between anaerobic and aerobic stages to select for polyphosphate accumulating organisms, and the AN/AE reactor degraded carbon and phosphorous. The second reactor (NIT) was operated with aerobic conditions to promote nitrifying bacteria and treat total ammonia nitrogen. The performance of this system for carbonaceous constituents and ammonia was evaluated by quantifying the kinetics, biofilm morphology, thickness, dry-mass, and dry-density of the two SB-MBBR in series technology. The AN/AE reactor achieved 97.5 +/- 1.7%, 58.8 +/- 5%, and 49 +/- 1% soluble chemical oxygen demand, total nitrogen, and total phosphorous removal efficiencies respectively. The NIT reactor achieved 98.7 +/- 2.4 % total ammonia nitrogen removal, though partial nitritation at rates of 1.09 +/- 0.03 g-N center dot m-2d-1, indicating this system can be incorporated in an anammox system. The study demonstrates that enhanced biological phosphorous removal, and potentially anaerobic removal of ammonia can be achieved for on-site treatment of cheese production wastewater.
引用
收藏
页数:9
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