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Performance of Compact Bio-Contact Oxidation Reactors for Municipal Wastewater Treatment Under Different Hydraulic Retention Time

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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
This study employed a laboratory-scale continuous upflow bio-contact oxidation reactor to treat 50 L/day of municipal wastewater in Al Rumaitha City, located north of Al Muthanaa Province in Iraq. The reactor configuration consisted of two anoxic-aerobic reactors nested inside each other, with a 1:3 volume ratio of anoxic to aerobic zones. Both the anoxic and aerobic reactors were loaded with K1 bio-media, filling them to 50% capacity for fixing and preserving the biomass. The reactors were operated in a mode that achieved full nitrification-denitrification without any sludge return, relying solely on internal recycling from the aerobic to the anoxic reactor. After biofilm formation on the carriers, three distinct hydraulic retention times (HRTs) were investigated – ranging from 24 to 12 hours – to evaluate their impact on removing biological nutrients from municipal sewage. In this operational approach, the preferred internal recycle ratio and gas/water ratio for effective nitrogen removal were a complete feed rate recycle of 100% and a ratio of 1:5, respectively. The experiment results highlighted that a 24-hour hydraulic retention time was most suitable for the simultaneous removal of organic carbon (COD) and nutrients. During this period, average removal efficiencies were found to be 93.51% for COD, 94.50% for ammonium (NH4+), 60.98% for total nitrogen (TN), and 67.57% for total phosphorus (TP). Furthermore, the aerobic bio-contact oxidation reactors maintained an average dissolved oxygen (DO) concentration of 4.89 mg/L. In contrast, the anoxic bio- contact oxidation reactors exhibited a lower average DO concentration of 0.38 mg/L.
Rocznik
Strony
304--318
Opis fizyczny
Bibliogr. 47 poz., rys., tab.
Twórcy
  • Department of Civil Engineering, College of Engineering, University of Basrah, Basrah, Iraq
  • Department of Civil Engineering, College of Engineering, University of Basrah, Basrah, Iraq
  • Department of Civil Engineering, College of Engineering, University of Basrah, Basrah, Iraq
Bibliografia
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  • 39. Sousa J.T., Foresti E. 1999. Environmental management and control. Use of anaerobic sludge as external carbon source of denitrification of wastewaters. Brazilian Journal of Agricultural and Environmental Engineering, 3, 69-73. Campina Grande/Paraíba: DEAg/UFPB, 1999 (In Portuguese).
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  • 44. Wang R.C., Wen, X.-H.; Qian, Y. 2005. Influence of carrier concentration on the performance and microbial characteristics of a suspended carrier biofilm reactor. Process Biochemistry, 40(9), 2992–3001.
  • 45. Xu S., Wu D., Hu Z. 2014. Impact of hydraulic retention time on organic and nutrient removal in a membrane coupled sequencing batch reactor. Water Research, 55: 12-20.
  • 46. Zafarzadeh A., Bina B., Nikaeen M., Attar H.M., Nejad M.H. 2010. Performance of moving bed biofilm reactors for biological nitrogen compounds removal from wastewater by partial nitrification-denitrification process. Iran J Environ Health Sci Eng 7(4): 353.
  • 47. Zilli R.P. 2013. Influence of hydraulic retention time and surface air velocity on the performance of a moving bed reactor with attached biofilm (MBBR). Thesis of Master in Chemical Engineering, Federal University of Santa Catarina, Florianopolis, p. 39.
Uwagi
Opracowanie rekordu ze środków MNiSW, umowa nr SONP/SP/546092/2022 w ramach programu "Społeczna odpowiedzialność nauki" - moduł: Popularyzacja nauki i promocja sportu (2024).
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-f7d964b4-8624-4009-8a92-d8552833685d
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