Trickling Filter for High Efficiency Treatment of Dairy Sewage

• Autorzy: Żyłka R. , Dąbrowski W. , Gogina E. , Yancen O.

Identyfikatory

DOI

10.12911/22998993/89657

• Języki publikacji: EN

Abstrakty

EN

The article presents the results of the research on the possibility of using a trickling filter for high efficiency treatment of dairy sewage. Nowadays, to the best of the authors’ knowledge, it is possible to change the activated sludge system to the trickling filter technology, especially in small dairy plants with lower raw sewage parameters in comparison to larger plants. In the research, dairy wastewater after dissolved air flotation (DAF) process was treated with a laboratory scale Gunt CE701e research model which allows to control the basic parameters of the treatment with a trickling filter (TF). The conducted study included determining the changing sewage parameters during the DAF process, as well as the trickling filter (TF) efficiency. Such parameters as Biological Oxygen Demand (BOD), Chemical Oxygen Demand (COD), total Organic Carbon (TOC), total Kjeldahl nitrogen (TKN) and total phosphorous (TP) were checked. The research results confirmed the possibility of high efficiency treatment of dairy sewage with DAF and trickling filter technologies. The average efficiency of DAF treatment was 59.3% for BOD, 49.0% for COD and 80.0% for TP, while the average treatment efficiency of TF was 87.3%, 78.3% and 27.9% without recirculation and 95.2%, 85.5% and 42.0% with 100% recirculation applied, respectively. The load of TF during the operation without recirculation was on average 0.22 kgBOD₅∙m^-3∙d^-1 and 0.25 with 100% recirculation. Applying recirculation allowed to reach the BOD, COD and total phosphorus standards for the sewage discharged to a receiver from Bielmlek dairy WWTP. On the other hand, the concentration of total nitrogen exceeded the permitted standards in this facility.

Słowa kluczowe

EN

dairy sewage; trickling filter; dissolved air flotation; efficiency

• Wydawca: Polskie Towarzystwo Inżynierii Ekologicznej ; Lublin University of Technology
• Czasopismo: Journal of Ecological Engineering
• Rocznik: 2018
• Tom: Vol. 19, nr 4
• Strony: 269--275
• Opis fizyczny: Bibliogr. 26 poz., rys., tab.

Twórcy

autor

Żyłka R.

• Bialystok University of Technology, Faculty of Building and Environmental Engineering, ul. Wiejska 45E, 15-351 Białystok, Poland

autor

Dąbrowski W.

• Bialystok University of Technology, Faculty of Building and Environmental Engineering, ul. Wiejska 45E, 15-351 Białystok, Poland

autor

Gogina E.

• Moscow State University of Civil Engineering, Yaroslawskoyoe Shosse, Moscow, Russia

autor

Yancen O.

• Moscow State University of Civil Engineering, Yaroslawskoyoe Shosse, Moscow, Russia

Bibliografia

• 1. Al-Shamrani A. A., James A., Xiao H. 2002. Destabilisation of oil–water emulsions and separation bydissolved air flotation. Water Research, 36: 1503-1512.
• 2. American Public Health Association (APHA). 2005. Standard Methods for Examination of Water and Wastewater. 21st edition. American Public Health Association. Washington
• 3. Babatola J. O., Oladepo K. T., Lukman S., Olarinoye N. O., Oke I. A. 2011. Failure Analysis of a Dissolved Air Flotation Treatment Plant in a Dairy Industry. Journal of Failure Analysis and Prevention. 11: 110-122.
• 4. Daigger G. T., Boltz J. P. 2011. Trickling Filter and Trickling Filter-Suspended Growth Process Design and Operation: A State of Art Review. Water Environmental Research. 83(5), 388-404.
• 5. Danalewich J. R., Papagiannis T. G., Belyea R. L., Tumbleson, M. E., Raskina L. 1998. Characterization of dairy waste streams, current treatment practices, and potential for biological nutrient removal. Water Research. 32(12), 3555-3568.
• 6. Dąbrowski W. 2011. Determination of pollutants concentration changes during dairy wastewater treatment in Mlekovita Wysokie Mazowieckie. Ecological Engineering. 24, 236-243 (In Polish).
• 8. Dąbrowski W., Żyłka R., Rynkiewicz M. 2016. Evaluation of energy consumption in agro-industrial wastewater treatment plant. Journal of Ecological Engineering. 17: 73-78.
• 9. Dąbrowski W., Żyłka R. 2015. Evaluation of energy consumption in dairy WWTP Bielmlek Bielsk Podlaski. Ecological Engineering. 43, 68-74 (In Polish).
• 10. Godoy-Olmos S., Martinez-Lloren S., Tomas-Vidal A., Jover-Cerda M. 2016. Influence of filter medium type, temperature and ammonia production on nitrifying trickling filters performance. Journal of Environmental Chemical Engineering. 4, 328-340.
• 11. Gogina E., Yantsen O. 2015. Research of biofilter feed properties. International Journal of Applied Engineering Research. 10(24), 44070-44074.
• 12. Habte Lemji H., Eckstädt H. 2013. A pilot scale trickling filter with pebble gravel as media and its performance to remove chemical oxygen demand from synthetic brewery wastewater. Journal of Zhejiang University – SCIENCE B (Biomedicine & Biotechnology). 14(10), 924-933,
• 13. Henrich C. D., Marggraff M. 2013. Energy-efficient Wastewater Reuse – The Renaissance of Trickling Filter Technology. Proc. 9th International Conference on Water Reuse, 27-31.
• 14. Henrich C. D. 2014. German research underway on trickling filter practices. World Water – Wastewater Treatment. 9-10/2014, 37-38.
• 15. Integrated Pollution Prevention and Control (IPPC) Permission for Bielmlek Dairy Cooperative WWTP. 2015. (In Polish).
• 16. Kanda R., Kishimoto N., Hinobayashi J., Hashimoto T. 2016. Effects of recirculation rate of nitrified liquor and temperature on biological nitrification–denitrification process using a trickling filter. Water and Environment Journal. 30, 190-196.
• 17. Łobos-Moysa E., Bod M., Śliwa A. 2016. Influence of modified porous aggregates on the efficiency of treatment by trickling filter systems. Proceedings of ECOpole. 10(2), 693-698. (In Polish)
• 18. Tchobanoglous, G. 1997. Wastewater Engineering: Treatment, Disposal and Reuse, 2nd edition, Mc Graw Hill, New York
• 19. Obarska-Pempkowiak H., Gajewska M., Wojciechowska E. 2010. Wetland treatment of water and wastewater. PWN Publishing, Warsaw (In Polish).
• 20. Dymaczewski Z., Oleszkiewicz J. A., Sozański M. 1997. Wastewater treatment plant exploiter’s guide. PZiTS, Poznań (In Polish).
• 21. Passeggi M., López I., Borzacconi L. 2012. Modified UASB reactor for dairy industry wastewater: performance indicators and comparison with the traditional approach. Journal of Cleaner Production. 26, 90-94.
• 22. Post T., Medlock J. 2002. Wastewater Technology Fact Sheet Tricking Filters, EPA
• 23. Regulations of the Minister of Environment from 5th of November 1991 on conditions to be met for disposal of treated sewage into water and soil (Dz. U. 116, no. 503). (In Polish).
• 24. Regulations of the Minister of Environment from 18th of November 2014 on conditions to be met for disposal of treated sewage into water and soil and concerning substances harmful to the environment (Dz.U. 2014. no. 1800). (In Polish).
• 25. Rodziewicz J., Janczukowicz W., Mielcarek A., Filipkowska U., Kłodowska I., Ostrowska K., Duchniewicz S. (2014). Anaerobic rotating disc batch reactor nutrient removal process enhanced by volatile fatty acid adsorption. Environmental Technology. 36(8), 953-958.
• 26. Rusten B., Lundar A., Eide O., Ødegaard H. 1993. Chemical Pretreatment of Dairy Wastewater. Water Science and Technology. 28(2): 67-76.
• 27. U.S Environmental Protection Agency (EPA). 2000. Wastewater Technology Fact Sheet – Trickling filters. Office of Water, Washington D.C.

Uwagi

Błędna numeracja w bibliografii.