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Evaluation of High Rate MBBR to Predict Optimal Design Parameters for Higher Carbon and Subsequent Ammoniacal Nitrogen Removal


Affiliations
1 Department of Technology, Savitribai Phule Pune University, Pune - 411 007, India
2 COE Biotechnology, R.D. Aga Research, Technology and Innovation Centre, Thermax Ltd, Pune - 411 019, India
 

The high rate moving bed biofilm reactor (MBBR) processes were designed for wastewater treatment to meet the past effluent discharge norms of biological oxygen demand (BOD) <50 mg/l. However, they are incapable of meeting current effluent discharge norms which consist of BOD <10 mg/l and total nitrogen <10 mg/l. This study analyses the effect and variation of organic loading rate from 1.21 kg to 4.59 kg chemical oxygen demand (COD)/(m3 day) and surface loading rate from 4.9 g to 24 g COD/(m2 day) on a high rate MBBR performance. The results of COD reduction (CODred) and subsequent ammoniacal nitrogen reduction (NH3–Nred) were in the range of 65.4% to 87.8% and 11.8% to 47.2% respectively. The projected graphical optimization defines the design parameters for MBBR and also predicts CODred and subsequent NH3–Nred. By understanding this subsequent NH3–Nred in the MBBR system, future designs for engineering technologies will be aided.

Keywords

Graphically, HRT, MBBR, Optimized, Organic Load, Wastewater.
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  • Loukidou, M. X. and Zouboulis, A. I., Comparison of two biological treatment processes using attached-growth biomass for sanitary landfill leachate treatment. Environ. Pollut., 2001, 111, 273-281.

  • Schmidt, T. M. and Schaechter, M., Topics in Ecological and Environmental Microbiology, Elsevier/Academic Press, Amsterdam, Boston, 2012.

  • Magdum, S. S. and Kalyanraman, V., Existing biological nitrogen removal processes and current scope of advancement. Res. J. Chem. Environ., 2017, 21, 43-53.

  • Ødegaard, H., Gisvold, B. and Strickland, J., The influence of carrier size and shape in the moving bed biofilm process. Water Sci. Technol., 2000, 41, 383-391.

  • Barwal, A. and Chaudhary, R., To study the performance of biocarriers in moving bed biofilm reactor (MBBR) technology and kinetics of biofilm for retrofitting the existing aerobic treatment systems: a review. Rev. Environ. Sci. Bio/Technol., 2014, 13, 285- 299.

  • Odegaard, H., Innovations in wastewater treatment: the moving bed biofilm process. Water Sci. Technol., 2006, 53, 17-33.

  • Gu, Q., Sun, T., Wu, G., Li, M. and Qiu, W., Influence of carrier filling ratio on the performance of moving bed biofilm reactor in treating coking wastewater. Bioresour. Technol., 2014, 166, 72- 78.

  • Torkaman, M., Borghei, S. M., Tahmasebian, S. and Andalibi, M. R., Nitrogen removal from high organic loading wastewater in modified Ludzack-Ettinger configuration MBBR system. Water Sci. Technol., 2015, 72, 1274-1282.

  • Bassin, J. P., Dias, I. N., Cao, S. M. S., Senra, E., Laranjeira, Y. and Dezotti, M., Effect of increasing organic loading rates on the performance of moving-bed biofilm reactors filled with different support media: Assessing the activity of suspended and attached biomass fractions. Process Saf. Environ. Prot., 2016, 100, 131- 141.

  • Joshi, S., MBBR. Shrishti Eco-Research Institute, 2015; https:// sswm.info/step-nawatech/module-1-nawatech-basics/appropriate-technologies0/mbbr (accessed on 30 January 2019).

  • CPCB, Inventorization of Sewage Treatment Plant, Delhi, 2015; https://nrcd.nic.in/writereaddata/FileUpload/NewItem_210_Inventorization_ of_Sewage-Treatment_Plant.pdf (accessed on 17 June 2017).

  • APHA, Standard Methods for the Examination of Water and Wastewater, American Water Works Association/American Public Works Association/Water Environment Federation, 2012, 22nd edn.

  • Li, Y. M., Gu, G. W., Zhao, J. F., Yu, H. Q., Qiu, Y. L. and Peng, Y. Z., Treatment of coke-plant wastewater by biofilm systems for removal of organic compounds and nitrogen. Chemosphere, 2003, 52, 997-1005.

  • Almomani, F. A. and Khraisheh, M. A. M., Treatment of septic tank effluent using moving-bed biological reactor: kinetic and biofilm morphology. Int. J. Environ. Sci. Technol., 2016, 13, 1917-1932.

  • Shrestha, A., Specific Moving Bed Biofilm Reactor in Nutrient Removal from Municipal Wastewater, Master thesis, University of Technology, Sydney, Australia, 2013.

  • Kawan, J. A., Abd-Rahman, R., bin Jaafar, O. and Suja, F., Polishing of chemical oxygen demand (COD) using moving bed bio-reactor. Appl. Mech. Mater., 2015, 773-774, 1281-1285.

  • Almomani, F. A., Delatolla, R. and Örmeci, B., Field study of moving bed biofilm reactor technology for post-treatment of wastewater lagoon effluent at 1°C. Environ. Technol., 2014, 35, 1596-1604.

  • Melin, E., Leiknes, T., Helness, H., Rasmussen, V. and Odegaard, H., Effect of organic loading rate on a wastewater treatment process combining moving bed biofilm and membrane reactors. Water Sci. Technol., 2005, 51, 421-430.


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  • Evaluation of High Rate MBBR to Predict Optimal Design Parameters for Higher Carbon and Subsequent Ammoniacal Nitrogen Removal

Abstract Views: 296  |  PDF Views: 98

Authors

Sandip Magdum
Department of Technology, Savitribai Phule Pune University, Pune - 411 007, India
V. Kalyanraman
COE Biotechnology, R.D. Aga Research, Technology and Innovation Centre, Thermax Ltd, Pune - 411 019, India

Abstract


The high rate moving bed biofilm reactor (MBBR) processes were designed for wastewater treatment to meet the past effluent discharge norms of biological oxygen demand (BOD) <50 mg/l. However, they are incapable of meeting current effluent discharge norms which consist of BOD <10 mg/l and total nitrogen <10 mg/l. This study analyses the effect and variation of organic loading rate from 1.21 kg to 4.59 kg chemical oxygen demand (COD)/(m3 day) and surface loading rate from 4.9 g to 24 g COD/(m2 day) on a high rate MBBR performance. The results of COD reduction (CODred) and subsequent ammoniacal nitrogen reduction (NH3–Nred) were in the range of 65.4% to 87.8% and 11.8% to 47.2% respectively. The projected graphical optimization defines the design parameters for MBBR and also predicts CODred and subsequent NH3–Nred. By understanding this subsequent NH3–Nred in the MBBR system, future designs for engineering technologies will be aided.

Keywords


Graphically, HRT, MBBR, Optimized, Organic Load, Wastewater.

References





DOI: https://doi.org/10.18520/cs%2Fv116%2Fi12%2F2083-2088