Start-up and operation of single-stage autotrophic nitrogen removal process in upflow double layer filler reactor
LI Yu-qi1, XIANG Tao1, GAO Da-wen1, PENG Yong-zhen2
1. School of Environment, State Key Laboratory of Urban Water Resource and Environment, Harbin Institute of Technology, Harbin 150006, China;
2. College of Environmental and Energy Engineering, 100124 Beijing, China
The start-up and operation of single-stage autotrophic nitrogen removal process in upflow double layer filler reactor were successfully established in this study after 139 days. Zeolite and polyurethane foam were used as reactor filler. Synthetic high ammonia nitrogen (110~130mg/L) wastewater was fed to the reactor. Ratio of filler zeolite and polyurethane foam height in No.1and No.2 reactor was 2:3 and 3:2, resprctively. The results showed that the total nitrogen removal efficiency of No.1reactor reached 84.4%, while in the No.2 reactor 81.8%, with a total nitrogen removal load achieved 0.15 and 0.14kgN/(m3·d), respectively. Without adding organic matter into influent, compared with No. 1reactor, △NO3--N/△NH4+-N of No.2 reactor has been stable around 0.11. The total nitrogen removal efficiency of two reactors both increased with the addition of organic carbon source. It was indicated that appropriate concentration of COD can enhance autotrophic nitrogen removal performance. After backwashing, the NO3--N concentration of No. 1 reactor decreased from 17.61mg/L to below 10mg/L. It was showed that backwashing can effectively wash out NOB, and the combination of backwashing and other NOB suppression strategies can better maintain the long-term stable operation of single-stage autotrophic nitrogen removal process.
Third K A, Sliekers A O, Kuenen J G, et al. The CANON system (Completely Autotrophic Nitrogen-removal Over Nitrite) under ammonium limitation:interaction and competition between three groups of bacteria[J]. Systematic & Applied Microbiology, 2001,24(4):588-596.
[2]
Lackner S, Gilbert E M, Vlaeminck S E, et al. Full-scale partial nitritation/anammox experiences——an application survey[J]. Water Research, 2014,55(10):292-303.
[3]
Arriagada C, Guzmán-Fierro V, Giustinianovich E, et al. NOB suppression and adaptation strategies in the partial nitrification-Anammox process for a poultry manure anaerobic digester[J]. Process Biochemistry, 2017,58:258-265.
[4]
Vázquezpadín J R, Pozo M J, Jarpa M, et al. Treatment of anaerobic sludge digester effluents by the CANON process in an air pulsing SBR[J]. Journal of Hazardous Materials, 2009,166(1):336-341.
[5]
Zhang F Z, Peng Y, Miao L, et al. A novel simultaneous partial nitrification Anammox and denitrification (SNAD) with intermittent aeration for cost-effective nitrogen removal from mature landfill leachate[J]. Chemical Engineering Journal, 2017,313:619-628.
[6]
Azari M, Walter U, Rekers V, et al. More than a decade of experience of landfill leachate treatment with a full-scale anammox plant combining activated sludge and activated carbon biofilm[J]. Chemosphere, 2017,174:117.
[7]
Strous M, Heijnen J J, Kuenen J G, et al. The sequencing batch reactor as a powerful tool for the study of slowly growing anaerobic ammonium-oxidizing microorganisms[J]. Applied Microbiology & Biotechnology, 1998,50(5):589-596.
Wang S B, Peng Y L. Natural zeolites as effective adsorbents in water and wastewater treatment[J]. Chemical Engineering Journal, 2010, 156(1):11-24.
[12]
Yapsakli K, Aktan C K, Mertoglu B. Anammox-zeolite system acting as buffer to achieve stable effluent nitrogen values[J]. Biodegradation, 2016,28(1):1-11.
[13]
国家环境保护总局.水和废水监测分析方法[M]. 北京:中国环境科学出版社, 2002.
[14]
Gonzalez-Martinez A, Rodriguez-Sanchez A, Garcia-Ruiz M J, et al. Performance and bacterial community dynamics of a CANON bioreactor acclimated from high to low operational temperatures[J]. Chemical Engineering Journal, 2016,287:557-567.
[15]
Wang Y, Wang Y, Wei Y, et al. In-situ restoring nitrogen removal for the combined partial nitritation-anammox process deteriorated by nitrate build-up[J]. Biochemical Engineering Journal, 2015,98:127-136.
[16]
Abeling U, Seyfried C F. Anaerobic-aerobic treatment of high-strength ammonium wastewater-nitrogen removal via nitrite[J]. Water Science & Technology, 1992,26(5/6):1007-1015.
[17]
Hellinga C, Schellen A A J C, Mulder J W, et al. The sharon process:An innovative method for nitrogen removal from ammonium-rich waste water[J]. Water Science & Technology, 1998,37(9):135-142.
Anthonisen A C, Loehr R C, Prakasam T B, et al. Inhibition of nitrification by ammonia and nitrous acid[J]. Journal Water Pollution Contral Federation, 1976,48(5):835-852.
Daverey A, Su S H, Huang Y T, et al. Partial nitrification and anammox process:a method for high strength optoelectronic industrial wastewater treatment[J]. Water Research, 2013,47(9):2929-2937.
Misaelides P. Application of natural zeolites in environmental remediation:A short review[J]. Microporous & Mesoporous Materials, 2011,144(1):15-18.
[28]
Zhang X, Li D, Liang Y, et al. Performance and microbial community of completely autotrophic nitrogen removal over nitrite (CANON) process in two membrane bioreactors (MBR) fed with different substrate levels[J]. Bioresource Technology, 2014,152(1):185-191.