Abstract
Accumulation of nitrite in shortcut nitrification is influenced by several factors including dissolved oxygen concentration (DO), pH, temperature, free ammonia (FA), and free nitrous acid (FNA). In this study, a model based on minimum dissolved oxygen concentration (DOmin), minimum/maximum substrate concentration (Smin and Smax), was developed. The model evaluated the influence of pH (7–9), temperature (10–35 °C), and solids retention time (SRT) (5 days–infinity) on MSC values. The evaluation was conducted either by controlling total ammonium nitrogen (TAN) or total nitrite nitrogen (TNN), concentration at 50 mg N/L while allowing the other to vary from 0 to 1000 mg N/L. In addition, specific application for shortcut nitrification-anammox process at 10 °C was analyzed. At any given operational condition, the model was able to predict if shortcut nitrification can be achieved and provide the operational DO range which is higher than the DOmin of AOB and lower than that of NOB. Furthermore, experimental data from different literature studies were taken for model simulation and the model prediction fit well the experiment. For the Sharon process, model prediction with default kinetics did not work but the model could make good prediction after adjusting the kinetic values based on the Sharon-specific kinetics reported in the literature. The model provides a method to identify feasible combinations of pH, DO, TAN, TNN, and SRT for successful shortcut nitrification.


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Discover the latest articles and news from researchers in related subjects, suggested using machine learning.Abbreviations
- AOB:
-
Ammonia-oxidizing bacteria
- BNR:
-
Biological nitrogen removal
- CSTR:
-
Continuous stirred-tank reactor
- DO:
-
Dissolved oxygen concentration
- DOmin :
-
Minimum DO concentration
- FA:
-
Free ammonia
- FNA:
-
Free nitrous acid
- MSC:
-
Minimum/maximum substrate concentration
- NOB:
-
Nitrite-oxidizing bacteria
- Smin :
-
Minimum substrate concentration
- Smax :
-
Maximum substrate concentration
- SRT:
-
Solids retention time
- TAN:
-
Total ammonium nitrogen
- TNN:
-
Total nitrite nitrogen
References
Anthonisen A, Loehr R, Prakasam T, Srinath E (1976) Inhibition of nitrification by ammonia and nitrous acid. Journal (Water Pollution Control Federation) 48:835–852
Beccari M, Passino R, Ramadori R, Tandoi V (1983) Kinetics of dissimilatory nitrate and nitrite reduction in suspended growth culture. Journal Water Pollution Control Federation 55:58–64
Boon B, Laudelout H (1962) Kinetics of nitrite oxidation by Nitrobacter winogradskyi. Biochem J 85:440
Chen JW, Zheng P, Yu Y, Mahmood Q, Tang CJ (2010) Enrichment of high activity nitrifers to enhance partial nitrification process. Bioresour Technol 101(19):7293–7298
Chuang HP, Ohashi A, Imachi H, Tandukar M, Harada H (2007) Effective partial nitrification to nitrite by down-flow hanging sponge reactor under limited oxygen condition. Water Res 41(2):295–302
Chung J, Bae W, Lee YW, Rittmann BE (2007) Shortcut biological nitrogen removal in hybrid biofilm/suspended growth reactors. Process Biochem 42(3):320–328
Ciudad G, Rubilar O, Munoz P, Ruiz G, Chamy R, Vergara C, Jeison D (2005) Partial nitrification of high ammonia concentration wastewater as a part of a shortcut biological nitrogen removal process. Process Biochem 40(5):1715–1719
De Clippeleir H, Vlaeminck SE, De Wilde F, Daeninck K, Mosquera M, Boeckx P, Verstraete W, Boon N (2013) One-stage partial nitritation/anammox at 15 °C on pretreated sewage: feasibility demonstration at lab-scale. Appl Microbiol Biotechnol 97:10199–10210
Fux C, Huang D, Monti A, Siegrist H (2004) Difficulties in maintaining long-term partial nitritation of ammonium-rich sludge digester liquids in a moving-bed biofilm reactor (MBBR). Water Sci Technol 49(11–12):53–60
Galí A, Dosta J, van Loosdrecht MCM, Mata-Alvarez J (2006) Biological nitrogen removal via nitrite of reject water with a SBR and chemostat SHARON/denitrification process. Ind Eng Chem Res 45(22):7656–7660
Galí A, Dosta J, Mace S, Mata-Alvarez J (2007a) Comparison of reject water treatment with nitrification/denitrification via nitrite in SBR and SHARON chemostat process. Environ Technol 28(2):173–176
Galí A, Dosta J, van Loosdrecht MCM, Mata-Alvarez J (2007b) Two ways to achieve an anammox influent from real reject water treatment at lab-scale: partial SBR nitrification and SHARON process. Process Biochem 42:715–720
Guo JH, Peng YZ, Wang SY, Zheng YN, Huang HJ, Ge SJ (2009) Effective and robust partial nitrification to nitrite by real-time aeration duration control in an SBR treating domestic wastewater. Process Biochem 44:979–985
Hellinga C, Schellen A, Mulder J, Van Loosdrecht M, Heijnen J (1998) The SHARON process: an innovative method for nitrogen removal from ammonium-rich waste water. Water Sci Technol 37:135–142
Hellinga C, Van Loosdrecht M, Heijnen J (1999) Model based design of a novel process for nitrogen removal from concentrated flows. Math Comput Model Dyn Syst 5:351–371
Henze M, Grady Jr C, Gujer W, Marais G, Matsuo T (1987) Activated Sludge Model No. 1: IAWPRC Scientific and Technical Report No. 1. IAWPRC, London
Hu Z, Lotti T, de Kreuk M, Kleerebezem R, van Loosdrecht M, Kruit J, Jetten MS, Kartal B (2013) Nitrogen removal by a nitritation-anammox bioreactor at low temperature. Appl Environ Microbiol 79:2807–2812
Liu X, Kim M, Nakhla G (2016) Operational conditions for successful partial nitrification in an SBR based on process kinetics. Environ Technol (just-accepted), 1–27. doi:10.1080/09593330.2016.1209246
Lotti T, Kleerebezem R, Hu Z, Kartal B, Jetten M, van Loosdrecht M (2014) Simultaneous partial nitritation and anammox at low temperature with granular sludge. Water Res 66:111–121
Magri A, Corominas L, Lopez H, Campos E, Balaguer M, Colprim J, Flotats X (2007) A model for the simulation of the SHARON process: pH as a key factor. Environ Technol 28:255–265
Metcalf&Eddy (2014) Wastewater Engineering: Treatment and Resource Recovery. McGraw-Hill international ed.
Metcalf&Eddy (2003) Wastewater engineering: treatment, disposal, reuse, 4th edn. Inc., McGraw-Hill, New York
Park S, Bae W, Chung J, Baek S-C (2007) Empirical model of the pH dependence of the maximum specific nitrification rate. Process Biochem 42:1671–1676
Park S, Bae W (2009) Modeling kinetics of ammonium oxidation and nitrite oxidation under simultaneous inhibition by free ammonia and free nitrous acid. Process Biochem 44:631–640
Park S, Bae W, Rittmann BE (2010a) Operational boundaries for nitrite accumulation in nitrification based on minimum/maximum substrate concentrations that include effects of oxygen limitation, pH, and free ammonia and free nitrous acid inhibition. Environmental Science & Technology 44(1):335–342
Park S, Bae W, Rittmann BE, Kim S, Chung J (2010b) Operation of suspended-growth shortcut biological nitrogen removal (SSBNR) based on the minimum/maximum substrate concentration. Water Res 44(5):1419–1428
Persson F, Sultana R, Suarez M, Hermansson M, Plaza E, Wilén B-M (2014) Structure and composition of biofilm communities in a moving bed biofilm reactor for nitritation–anammox at low temperatures. Bioresour Technol 154:267–273
Rittmann BE, McCarty PL (1980) Model of steady-state-biofilm kinetics. Biotechnol Bioeng 22:2343–2357
Rittmann BE, McCarty PL (2001) Environmental biotechnology: principles and applications. McGraw-Hill
Ruiz G, Jeison D, Rubilar O, Ciudad G, Chamy R (2006) Nitrification-denitrification via nitrite accumulation for nitrogen removal from wastewaters. Bioresour Technol 97(2):330–335
Schramm A, de Beer D, van den Heuvel JC, Ottengraf S, Amann R (1999) Microscale distribution of populations and activities of Nitrosospira and Nitrospira spp. along a macroscale gradient in a nitrifying bioreactor: quantification by in situ hybridization and the use of microsensors. Appl Environ Microbiol 65(8):3690–3696
Sinha B, Annachhatre AP (2007) Assessment of partial nitrification reactor performance through microbial population shift using quinone profile, FISH and SEM. Bioresour Technol 98(18):3602–3610
Strous M, Van Gerven E, Zheng P, Kuenen JG, Jetten MS (1997) Ammonium removal from concentrated waste streams with the anaerobic ammonium oxidation (anammox) process in different reactor configurations. Water Res 31:1955–1962
Turk O, Mavinic DS (1987) Benefits of using selective-inhibition to remove nitrogen from highly nitrogenous wastes. Environ Technol Lett 8:419–426
Vadivelu VM, Keller J, Yuan Z (2006) Effect of free ammonia and free nitrous acid concentration on the anabolic and catabolic processes of an enriched Nitrosomonas culture. Biotechnol Bioeng 95:830–839
van Dongen U, Jetten MSM, van Loosdrecht MCM (2001) The SHARON((R))-anammox((R)) process for treatment of ammonium rich wastewater. Water Sci Technol 44:153–160
Van Hulle SW, Volcke EI, Teruel JL, Donckels B, van Loosdrecht M, Vanrolleghem PA (2007) Influence of temperature and pH on the kinetics of the Sharon nitritation process. J Chem Technol Biotechnol 82:471–480
van Kempen R, Mulder JW, Uijterlinde CA, Loosdrecht MCM (2001) Overview: full scale experience of the SHARON (R) process for treatment of rejection water of digested sludge dewatering. Water Sci Technol 44:145–152
Van Loosdrecht MCM, Jetten MSM (1998) Microbiological conversions in nitrogen removal. Water Sci Technol 38:1–7
Yan J, Hu YY (2009) Comparison of partial nitrification to nitrite for ammonium-rich organic wastewater in sequencing batch reactors and continuous stirred-tank reactor at laboratory-scale. Water Sci Technol 60:2861–2868
Acknowledgements
This work was supported by the National Science and Engineering Research council of Canada [grant number CRDPJ 458990-13].
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Responsible editor: Marcus Schul
Electronic supporting information (ESI): DO data for nitrite accumulation and model derivation.
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Liu, X., Kim, M. & Nakhla, G. A model for determination of operational conditions for successful shortcut nitrification. Environ Sci Pollut Res 24, 3539–3549 (2017). https://doi.org/10.1007/s11356-016-8017-y
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DOI: https://doi.org/10.1007/s11356-016-8017-y