Start-Up of a Combined Anaerobic/Partial Nitritation/ANAMMOX Process for High-Salt Mustard Wastewater Treatment

被引:29
作者
Chen, You-Peng [1 ,2 ]
Ma, Teng-Fei [1 ]
Hu, Xiao [1 ]
Fang, Fang [1 ]
Shen, Yu [2 ]
Yang, Ji-Xiang [2 ]
Guo, Jin-Song [2 ]
Bao, Zhen-Guo [1 ]
Yan, Peng [2 ]
机构
[1] Chongqing Univ, Three Gorges Reservoir Reg Ecoenvironm MOE, Key Lab, Chongqing 400045, Peoples R China
[2] Chinese Acad Sci, Chongqing Inst Green & Intelligent Technol, Key Lab Reservoir Aquat Environm CAS, Chongqing 400714, Peoples R China
基金
中国国家自然科学基金;
关键词
Combined process; Anaerobic; Anammox; Partial nitritation; High salinity; SEQUENCING BATCH REACTOR; TANNERY SOAK LIQUOR; FIXED-BED REACTOR; PARTIAL NITRIFICATION; BIOLOGICAL TREATMENT; NITROGEN REMOVAL; NITRITE ACCUMULATION; SALINE WASTEWATERS; AMMONIUM OXIDATION; ACTIVATED-SLUDGE;
D O I
10.1007/s12010-014-1247-x
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
To treat high salinity wastewater from the mustard pickling industry, a combined anaerobic, partial nitritation (PN), and anammox process was employed using three connected reactors: an anaerobic sequencing batch biofilm reactor (ASBBR) for anaerobic treatment, a sequencing batch reactor (SBR) for PN, and an upflow anaerobic sludge blanket (UASB) for anammox. The start-up of the three individual reactors was investigated. Results showed that each reactor started up successfully, notwithstanding the stepwise increase of influent salinity to about 16.1 g NaCl/L. In the ASBBR, 89.7 % of chemical oxygen demand in the influent was removed and organic nitrogen was converted to ammonium (NH4 (+)-N). The SBR performed well with NO3 (-)-N concentration of 4.9 mg/L and ratio of NO2 (-)-N to NH4 (+)-N at the range of 1.0 to 1.3 in the effluent, which favored the anammox process. After the start-up of the UASB, the anammox process also showed stability and efficiency with a high total nitrogen removal efficiency of 86.2 % under high salinity of 12.0 g NaCl/L and nitrogen loading rate of 258 mg/(L center dot day).
引用
收藏
页码:119 / 134
页数:16
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