4.5 Article

Evaluation of heterotrophic nitrite removal by a sulphide and acetate oxidizing mixed culture originated from an oil reservoir

Journal

JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY
Volume 87, Issue 3, Pages 410-417

Publisher

WILEY-BLACKWELL
DOI: 10.1002/jctb.2738

Keywords

heterotrophic nitrite removal; biokinetics; modeling; biofilm reactor

Funding

  1. Natural Sciences and Engineering Research Council of Canada (NSERC)
  2. Canada Foundation for Innovation (CFI)

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BACKGROUND: Shortcut biological nitrogen removal (SBNR) has attracted much attention in recent years due to lower aeration and chemical oxygen demand (COD) requirements, shorter residence time and smaller biomass production. In this work an oil reservoir denitrifying culture, with the ability to function under autotrophic and heterotrophic conditions was used for heterotrophic denitritation. Using freely suspended cells, effects of nitrite concentration (10-50 mmol L-1) and temperature (15-35 degrees C) on the kinetics of denitritation were investigated and a kinetic model was developed. Potential for enhancement of nitrite removal rate, and impacts of nitrite concentration and loading rate were investigated in a continuous biofilm reactor. RESULTS: Nitrite did not impose any inhibitory effect, even at the highest applied concentration of 50 mmol L-1. Increase of temperature in the range 15-35 degrees C enhanced the reduction rate significantly. Fitting the experimental data into the model developed, values of biokinetic coefficients (mu(max-NO2), KS-NO2, YX-NO2, YX-Ace-NO2 and E mu-(NO2)) were determined. In the biofilm reactor increases in nitrite loading rate (through flow rate or feed nitrite concentration) led to a linear increase of nitrite removal rate, with the highest removal rate of 140.6 mmol L-1 h(-1) achieved with a residence time of 0.19 h. CONCLUSION: The enrichment culture used in this study is not only a superior biocatalyst for simultaneous removal of sulphide, nitrate and BOD, it could also be used effectively in the denitritation step of an SBNR process. The kinetic model developed would certainly have beneficial applications in the design, operation and control of the SBNR process. (C) 2011 Society of Chemical Industry

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