NDLI: Combined autotrophic nitritation and bioelectrochemical-sulfur denitrification for treatment of ammonium rich wastewater with low C/N ratio

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Combined autotrophic nitritation and bioelectrochemical-sulfur denitrification for treatment of ammonium rich wastewater with low C/N ratio

Content Provider	World Health Organization (WHO)-Global Index Medicus
Author	Hang, Qianyu Wang, Haiyan Yuan, Quan Crittenden, John Liu, Haitao Zhou, Yuexi
Description	Country affiliation: China Author Affiliation: Wang H ( State Key Laboratory of Environmental Criteria and Risk Assessment, Chinese Research Academy of Environmental Sciences, No. 8 Da Yang Fang, Anwai, Chaoyang District, Beijing, 100012, China. wanghy@craes.org.cn.); Hang Q ( Research Center for Water Pollution Control Technology, Chinese Research Academy of Environmental Sciences, No. 8 Da Yang Fang, Anwai, Chaoyang District, Beijing, 100012, China. wanghy@craes.org.cn.); Crittenden J ( State Key Laboratory of Environmental Criteria and Risk Assessment, Chinese Research Academy of Environmental Sciences, No. 8 Da Yang Fang, Anwai, Chaoyang District, Beijing, 100012, China.); Zhou Y ( Research Center for Water Pollution Control Technology, Chinese Research Academy of Environmental Sciences, No. 8 Da Yang Fang, Anwai, Chaoyang District, Beijing, 100012, China.); Yuan Q ( School of Civil and Environmental Engineering, Georgia Institute of Technology, Atlanta, GA, 30332, USA.); Liu H ( Brook Byers Institute for Sustainable Systems, Georgia Institute of Technology, 828 West Peachtree Street NW, Atlanta, GA, 30332, USA.)
Abstract	A novel combined autotrophic nitritation and bioelectrochemical-sulfur denitrification (CANBSD) process was developed for treatment of synthetic ammonium-rich wastewater with low carbon/nitrogen ratio. Total nitrogen removal of the CANBSD was higher than 95 %, the effluent $SO_{4}^{2−}$ was lower than $1280 mg L^{−1},$ and the maximum nitrogen volumetric loading rate was $1.2 kg m^{−3} day^{−1}$ when (1) the influent $NH_{4}^{+}-N$ was lower than $1008 mg L^{−1},$ (2) hydraulic retention time was between 3.7 and 32 h, (3) the DO was between 0.5 and $1.2 mg L^{−1},$ (4) the pH was between 7.5 and 8.2, and (5) the temperature was between 28 and 30 °C. Both the $NH_{4}^{+}-N$ removal and conversion to $NO_{2}^{−}-N$ in the nitritation membrane reactor (NMBR) were maintained at about 50 %, and the residual $NH_{4}^{+}-N$ and accumulated $NO_{2}^{−}-N$ were subsequently treated in the bioelectrochemical-sulfur three-dimensional denitrification reactor. The CANBSD energy consumption was 0.13 and $3.4 kWh m^{−3},$ respectively, for influent $NH_{4}^{+}-N$ of 100 and $1000 mg L^{−1}.$ The energy consumption of CANBSD was close to that of partial nitritation-ANNMMOX.
ISSN	09441344
Issue Number	3
Volume Number	23
e-ISSN	16147499
Journal	Environmental Science and Pollution Research
Language	English
Publisher	Springer
Publisher Date	2016-02-01
Publisher Place	Germany
Access Restriction	One Nation One Subscription (ONOS)
Subject Keyword	Ammonium Compounds Chemistry Sulfur Waste Water Water Pollutants, Chemical Autotrophic Processes Carbon Denitrification Nitrogen Journal Article Research Support, Non-u.s. Gov't Discipline Environmental Science Discipline Environmental Chemistry
Content Type	Text
Resource Type	Article
Subject	Environmental Chemistry Health, Toxicology and Mutagenesis Pollution Medicine

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