Enhanced carbon and nitrogen removal performance of simultaneous anammox and denitrification (SAD) with mannitol addition treating saline wastewater

被引:17
|
作者
Yang, Zhenlin [1 ]
Zhu, Weiqiang [2 ]
Yu, Deshuang [1 ]
Bo, Yuntai [3 ]
Li, Jin [1 ]
机构
[1] Qingdao Univ, Sch Environm Sci & Engn, Qingdao 266071, Peoples R China
[2] Univ Antwerp, Dept Biosci Engn, Res Grp Sustainable Energy Air & Water Technol, Antwerp, Belgium
[3] State Ocean Adm, Yantai Marine Environm Monitoring Ctr Stn, Yantai, Peoples R China
基金
中国博士后科学基金; 中国国家自然科学基金;
关键词
simultaneous anammox and denitrification (SAD); mannitol; saline wastewater; kinetic analysis; sludge properties; COMPATIBLE SOLUTES; SUBSTRATE RATIO; GRANULAR SLUDGE; MEMBRANE BIOREACTORS; OXYTETRACYCLINE OTC; MONOD KINETICS; SHORT-TERM; NITRIFICATION; INHIBITION; REACTOR;
D O I
10.1002/jctb.5781
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
BACKGROUND Simultaneous anammox and denitrification (SAD) can remove carbon and nitrogen. However, its performance is suppressed under saline surroundings. In this work, mannitol was used to enhance a SAD process treating saline wastewater. RESULTS The optimum carbon and nitrogen removal was achieved at 0.2 mmol L-1 mannitol, during which ammonium removal efficiency (ARE), nitrite removal efficiency (NRE) and chemical oxygen demand (COD) removal efficiency were 96.95%, 93.70% and 90.05%, respectively. The maximum ammonium removal rate (ARR), nitrite removal rate (NRR) and the specific anammox activity (SAA) were increased by 25.49%, 55.84% and 33.83% with optimum addition (0.2 mmol L-1 mannitol) respectively. The diameter of sludge was enlarged with the addition of mannitol (<= 0.2 mmol L-1). The Tseng-Wayman model was more suitable to simulate the whole SAD process. The modified logistic model, the modified Boltzman model and the modified Gompertz model were all appropriate to describe nitrogen removal in a typical cycle with the addition of mannitol. CONCLUSION Mannitol was effective in enhancing a SAD process treating saline wastewater, and maximum nitrogen removal was achieved at mannitol = 0.2 mmol L-1. The Tseng-Wayman model satisfactorily predicted the whole SAD process treating saline wastewater with mannitol addition. (c) 2018 Society of Chemical Industry
引用
收藏
页码:377 / 388
页数:12
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