Nitrification of high strength ammonia wastewater and nitrite accumulation characteristics

2003 ◽  
Vol 47 (11) ◽  
pp. 45-51 ◽  
Author(s):  
D.J. Kim ◽  
J.S. Chang ◽  
D.I. Lee ◽  
D.W. Han ◽  
I.K. Yoo ◽  
...  

Biological nitrogen removal via the nitrite pathway in wastewater treatment is very important in saving the cost of aeration and as an electron donor for denitrification. Wastewater nitrification and nitrite accumulation were carried out in a biofilm airlift reactor with autotrophic nitrifying biofilm. The biofilm reactor showed almost complete nitrification and most of the oxidized ammonium was present as nitrite at the ammonium load of 1.5 to 3.5 kg N/m3·d. Nitrite accumulation was stably achieved by the selective inhibition of nitrite oxidizers with free ammonia and dissolved oxygen limitation. Stable 100% conversion to nitrite could also be achieved even under the absence of free ammonia inhibition on nitrite oxidizers. Batch ammonium oxidation and nitrite oxidation with nitrite accumulating nitrifying biofilm showed that nitrite oxidation was completely inhibited when free ammonia is higher than 0.2 mg N/L. However, nitrite oxidation activity was recovered as soon as the free ammonia concentration was below the threshold level when dissolved oxygen concentration was not the limiting factor. Fluorescence in situ hybridization analysis of cryosectioned nitrite accumulating nitrifying biofilm showed that the β-subclass of Proteobacteria, where ammonia oxidizers belong, was distributed outside the biofilm whereas the α-subclass of Proteobacteria, where nitrite oxidizers belong, was found mainly in the inner part of the biofilm. It is likely that dissolved oxygen deficiency or limitation in the inner part of the nitrifying biofilm, where nitrite oxidizers exist, is responsible for the complete shut down of the nitrite oxidizers activity under the absence of free ammonia inhibition.

1998 ◽  
Vol 38 (1) ◽  
pp. 141-148
Author(s):  
Ferhan Çeçen ◽  
Suna Ipek

Nitrification of ammonium nitrogen and urea nitrogen was studied in a submerged biofilm reactor. The reactor was operated as a fed-batch reactor to which an excessive mass loading was applied. The increases in TKN, ammonium-N, NOx-N and NO2-N concentrations inside the reactor were investigated to assess inhibitory behaviour under non-steady state conditions. The maximum ammonium oxidation rate was about 60 mg NH4-N/h that corresponded to a surface removal rate of 8.5 g NH4-N/m2.d. The major factor for nitrite accumulation was the presence of free ammonia. In the oxidation of urea where the free ammonia concentrations were very small no nitrite accumulation was observed. Overall, the results showed that the fed-batch reactor technique could be applied to a nitrifying biofilm reactor to evaluate the effect of slug doses in a short time period.


2005 ◽  
Vol 52 (10-11) ◽  
pp. 517-524 ◽  
Author(s):  
B. Fernández ◽  
A. Vilar ◽  
M. Ben ◽  
C. Kennes ◽  
M.C. Veiga

Nitrification via nitrite was studied in two aerobic reactors treating wastewater from an aminoplastic resin producing factory at HRT varying between 1.37–1.89 and 2.45–3.63 days. Both reactors were fed with concentrations of 366, 450, 1099 and 1899mg N-NH4+/L. In general in the reactor operated at a lower HRT, the nitritation percentage decreased from 87.2 to 21.6%, while the nitratation percentage remained always lower than 2.5% (except in the last period) when the ammonium concentration was increased. This behaviour could be due to the inhibition of the ammonium and nitrite oxidation produced by high free ammonia concentrations up to 179.3mg N-NH3/L. In the reactor operated at a higher HRT, the nitritation percentage decreased and the nitratation percentage increased from 88.6 to 39.6% and from 0.65 to 35.7%, respectively, due to an increase of the dissolved oxygen concentration from 0.76 to 1.02mg O2/L. However, when ammonium was fed at a concentration of 1898.7mg N-NH4+/L, the nitritation increased and the nitratation decreased, probably as a result of the accumulation of free ammonia up to 2.04mg N-NH3/L, meaning that nitrite oxidizers were inhibited. Nitrite build-up was observed after each modification of ammonium concentration in the feed.


1996 ◽  
Vol 34 (3-4) ◽  
pp. 371-378 ◽  
Author(s):  
F. Fdz-Polanco ◽  
S. Villaverde ◽  
P. A. Garcia

The combined effect of temperature, pH and ammonium concentration over the nitrite accumulation phenomena in situations of free ammonia inhibition, their effect over the ammonia and nitrite oxidizer microorganiisms influence over the nitrification, have been studied in an Up-flow Biological Aerated Filter (UBAF). The free ammonia inhibition effect highly depends on the values of pH, temperature and ammonium concentration. For the same specific free ammonia concentration different values of temperature, pH and ammonium concentration bring about different nitrite accumulations. In conditions of no free ammonia inhibition and low values of temperature and pH, high ammonium concentrations bring about a higher relative activity of ammonia oxidizer microorganisms of the filter increases the nitratation efficiency in zones close to the outlet and will favour the nitrite accumulation in situations of free ammonia inhibition.


2016 ◽  
Vol 100 (9) ◽  
pp. 4177-4187 ◽  
Author(s):  
Qianwen Sui ◽  
Chong Liu ◽  
Junya Zhang ◽  
Hongmin Dong ◽  
Zhiping Zhu ◽  
...  

1997 ◽  
Vol 26 (4) ◽  
pp. 1049-1055 ◽  
Author(s):  
R. V. Smith ◽  
L. C. Burns ◽  
R. M. Doyle ◽  
S. D. Lennox ◽  
B. H. L. Kelso ◽  
...  

Chemosphere ◽  
2012 ◽  
Vol 88 (2) ◽  
pp. 188-195 ◽  
Author(s):  
L.W. Jaroszynski ◽  
N. Cicek ◽  
R. Sparling ◽  
J.A. Oleszkiewicz

2004 ◽  
Vol 49 (11-12) ◽  
pp. 123-130 ◽  
Author(s):  
N. Bernet ◽  
O. Sanchez ◽  
P. Dabert ◽  
A. Olaïzola ◽  
J.J. Godon ◽  
...  

Biological ammonium oxidation was carried out in two inverse turbulent bed reactors fed with synthetic mineral wastewater containing a high ammonium concentration (100 mg N-NH4+/L). Both reactors were started-up and operated in the same conditions except for the solid carrier concentration: the solid hold-up ratios applied, defined as the ratios of static to expanded bed height, were 0.1 and 0.3 in reactors R10 and R30 respectively. These two solid hold-up ratios generate different particle-to-particle collision frequencies and, therefore, detachment forces. The influence of solid hold-up on biofilm growth and nitrifying performance was studied from a macroscopic (i.e. nitrate and/or nitrite production) and microbiological point of view. After 60 days of operation, both reactors contained the same amount of biomass. However, R10 produced only nitrate while nitrite accumulated in R30. A comparison of microbial populations in the reactors showed that R10 contained both ammonium and nitrite oxidizing populations such as Nitrosomonas and Nitrospira, whereas in R30, ammonium oxidizing populations were much greater than those of nitrite oxidizers. The major ammonium-oxidizing organism was not the same in both reactors.


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