Determination of biokinetic coefficients for an adsorption/bio-oxidation process on municipal wastewater in pilot-scale

Document Type : Original Article

Authors
Mostafa Hadei 1
Mohammadreza Aalipour 1
Ali Fatehizadeh 1
Hamid Reza Safavi 2
Mohammad Ghasemian 3
Ahmad Reza Sahbaei 3
Seyyed Mohammad Mousavi 3
Mohsen Ashjaa Zadeh 3
Mohammad Mehdi Amin 4
1 Department of Environmental Health Engineering, Student Research Center, School of Health, Isfahan University of Medical Sciences, Isfahan, Iran
2 Department of Civil Engineering, Research Institute for Water and Wastewater, Isfahan University of Technology, Isfahan, Iran
3 Environmental Research Center, Research Institute for Primordial Prevention of Noncommunicable Disease, Isfahan University of Medical Sciences, Isfahan, Iran
4 Environmental Research Center, Research Institute for Primordial Prevention of Noncommunicable Disease, Isfahan University of Medical Sciences, Isfahan; Isfahan Water and Wastewater Company, Isfahan, Iran
10.4103/2277-9183.170702
Abstract
Aims: The present study was carried out to determine biokinetic coefficients of a pilot-scale adsorption-bio-oxidation process. Materials and Methods: The pilot plant was simulated North wastewater treatment plant, Isfahan, Iran. The pilot plant was operated 135 days under different mixed liquor suspended solids (MLSS) concentrations in aeration tank. In each phase, MLSS value was kept constant to reach a steady state condition. B-stage has a higher hydraulic retention time and SRT than A-stage. Also, in order to determine influence of biokinetic parameters on the effluent substrate concentration, a sensitivity analysis was performed. Results: The coefficients Y, K d , K S , and μmax of A-stage were 1.34 mg VSS/mg sCOD, 0.17 d−1 , 8.61 mg/L, and 2.78 d−1 , respectively. Also, Y, K d , K S , and μmax of B-stage were 0.74 mg VSS/mg sCOD, 0.12 d−1 , 3.34 mg/L, and 71.94 d−1 , respectively. Sensitivity analysis showed that in the A-stage, all coefficients are directly proportional to the effluent sCOD concentration. In the B-stage, K d and K S are directly proportional, but μmax was inversely proportional to the effluent sCOD concentration. Conclusions: All coefficients were in the range of activated sludge coefficients that are mentioned in the literature, except μmax and K S of B-stage. However, K S value of B-stage was close to the desired range. Sensitivity analysis showed that μmax and K S have the most influence on effluent substrate concentration (sCOD).

Keywords

International Journal of Environmental Health Engineering (IJEHE)
Volume 4, November
Autumn 2015
Pages 1-6

  • Receive Date 27 January 2023