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Gulhan H, Dizaji RF, Hamidi MN, Abdelrahman AM, Basa S, Cingoz S, Koyuncu I, Guven H, Ozgun H, Ersahin ME, Dereli RK, Ozturk I. Modelling of high-rate activated sludge process: Assessment of model parameters by sensitivity and uncertainty analyses. Sci Total Environ 2024; 915:170102. [PMID: 38228239 DOI: 10.1016/j.scitotenv.2024.170102] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [Track Full Text] [Subscribe] [Scholar Register] [Received: 09/22/2023] [Revised: 12/29/2023] [Accepted: 01/09/2024] [Indexed: 01/18/2024]
Abstract
The objective of this study is to develop a mechanistic model to predict the long-term dynamic performance of High-Rate Activated Sludge (HRAS) process, including the removal of carbon (COD), nitrogen (N), and phosphorus (P). The model was formulated with inspiration from Activated Sludge Models No. 1 and 3 (ASM1 and ASM3) to incorporate essential mechanisms, such as adsorption and storage substrate, specific to HRAS systems. A stepwise protocol was followed for calibration with dynamic data from a pilot-scale HRAS plant. Sensitivity analysis identified influential model parameters, including maximum specific growth rate (μ), growth yield (YH), storage yield (YSTO), storage rate (kSTO), decay rate (b), and half saturation of the readily biodegradable substrate for growth (KS1). The calibrated model achieved prediction efficiencies above the normalized Mean Absolute Error (MAE) of 70 % for mixed liquor suspended solids (MLSS), total chemical oxygen demand (TCOD), soluble COD (SCOD), particulate COD (XCOD), total nitrogen (TN), ammonia nitrogen (SNH), total phosphorus (TP), soluble TP (STP), and particulate TP (XTP). Uncertainty analysis revealed that SCOD was underestimated. Based on the dynamic profiles of uncertainty bands and observed data, there is potential for improving the estimation of dynamic behavior in STP. The observed discrepancies may be attributed to variations in wastewater characteristics during the monitoring period, particularly concerning the phosphorus (P) fractions of the readily biodegradable substrate (SS) and soluble inerts (SI), which were not considered as dynamically changing parameters in the model.
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Affiliation(s)
- Hazal Gulhan
- Istanbul Technical University, Civil Engineering Faculty, Environmental Engineering Department, Ayazaga Campus, Maslak 34469, Istanbul, Turkey.
| | - Reza Faraji Dizaji
- Istanbul Technical University, Civil Engineering Faculty, Environmental Engineering Department, Ayazaga Campus, Maslak 34469, Istanbul, Turkey
| | - Muhammed Nimet Hamidi
- Istanbul Technical University, Civil Engineering Faculty, Environmental Engineering Department, Ayazaga Campus, Maslak 34469, Istanbul, Turkey
| | - Amr Mustafa Abdelrahman
- Istanbul Technical University, Civil Engineering Faculty, Environmental Engineering Department, Ayazaga Campus, Maslak 34469, Istanbul, Turkey
| | - Safak Basa
- ISKI, Istanbul Water and Sewerage Administration, Eyup 34060, Istanbul, Turkey
| | - Seyma Cingoz
- ISKI, Istanbul Water and Sewerage Administration, Eyup 34060, Istanbul, Turkey
| | - Ismail Koyuncu
- Istanbul Technical University, Civil Engineering Faculty, Environmental Engineering Department, Ayazaga Campus, Maslak 34469, Istanbul, Turkey; National Research Center on Membrane Technologies, Istanbul Technical University, 34469 Maslak, Istanbul, Turkey
| | - Huseyin Guven
- Istanbul Technical University, Civil Engineering Faculty, Environmental Engineering Department, Ayazaga Campus, Maslak 34469, Istanbul, Turkey
| | - Hale Ozgun
- Istanbul Technical University, Civil Engineering Faculty, Environmental Engineering Department, Ayazaga Campus, Maslak 34469, Istanbul, Turkey; National Research Center on Membrane Technologies, Istanbul Technical University, 34469 Maslak, Istanbul, Turkey
| | - Mustafa Evren Ersahin
- Istanbul Technical University, Civil Engineering Faculty, Environmental Engineering Department, Ayazaga Campus, Maslak 34469, Istanbul, Turkey; National Research Center on Membrane Technologies, Istanbul Technical University, 34469 Maslak, Istanbul, Turkey
| | - Recep Kaan Dereli
- University College Dublin, School of Chemical and Bioprocess Engineering, Belfield, Dublin 4, Ireland
| | - Izzet Ozturk
- Istanbul Technical University, Civil Engineering Faculty, Environmental Engineering Department, Ayazaga Campus, Maslak 34469, Istanbul, Turkey
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di Biase A, Kowalski MS, Devlin TR, Oleszkiewicz JA. Modeling of the attached and suspended biomass fractions in a moving bed biofilm reactor. Chemosphere 2021; 275:129937. [PMID: 33636521 DOI: 10.1016/j.chemosphere.2021.129937] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 05/20/2020] [Revised: 01/16/2021] [Accepted: 02/06/2021] [Indexed: 06/12/2023]
Abstract
The performance, kinetics, and stoichiometry of three high-rate moving bed biofilm reactors (MBBRs) were evaluated. A constant surface area loading rate (SALR) and three different hydraulic retention times (HRTs) were utilized to create scenarios where the attached and suspended biomass fractions would differentiate, despite the main design parameter remaining constant. Performance was simulated using BioWin™ 6.0 software. The objective was to evaluate whether a calibrated/validated model could accurately predict experimental results. Initially, a sensitivity analysis was performed to determine influential parameters. The calibration/validation of influential parameters was then conducted via steady-state simulations for two base cases: 1) highest HRT; and 2) lowest HRT. Both sets of calibrated/validated parameters were substantiated using: 1) steady-state simulations at the other HRTs; and 2) dynamic simulations to evaluate the kinetic rates of attached and suspended biomass fractions at all HRTs. Results demonstrated that the model could be calibrated/validated for a single HRT, but could not accurately predict the performance, kinetics, or stoichiometry at other HRTs.
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Affiliation(s)
- Alessandro di Biase
- Department of Civil Engineering, University of Manitoba, Winnipeg, R3T 5V6, Canada.
| | - Maciej S Kowalski
- Department of Civil Engineering, University of Manitoba, Winnipeg, R3T 5V6, Canada
| | - Tanner R Devlin
- Department of Civil Engineering, University of Manitoba, Winnipeg, R3T 5V6, Canada; Nexom, Winnipeg, R2J 3R8, Canada
| | - Jan A Oleszkiewicz
- Department of Civil Engineering, University of Manitoba, Winnipeg, R3T 5V6, Canada
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Moretti P, Choubert JM, Canler JP, Buffière P, Pétrimaux O, Lessard P. Dynamic modeling of nitrogen removal for a three-stage integrated fixed-film activated sludge process treating municipal wastewater. Bioprocess Biosyst Eng 2017; 41:237-247. [PMID: 29127499 DOI: 10.1007/s00449-017-1862-3] [Citation(s) in RCA: 7] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 06/22/2017] [Accepted: 11/02/2017] [Indexed: 10/18/2022]
Abstract
The integrated fixed-film activated sludge (IFAS) process is being increasingly used to enhance nitrogen removal for former activated sludge systems. The aim of this work is to evaluate a numerical model of a new nitrifying/denitrifying IFAS configuration. It consists of two carrier-free reactors (anoxic and aerobic) and one IFAS reactor with a filling ratio of 43% of carriers, followed by a clarifier. Simulations were carried out with GPS-X involving the nitrification reaction combined with a 1D heterogeneous biofilm model, including attachment/detachment processes. An original iterative calibration protocol was created comprising four steps and nine actions. Experimental campaigns were carried out to collect data on the pilot in operation, specifically for modelling purpose. The model used was able to predict properly the variations of the activated sludge (bulk) and the biofilm masses, the nitrification rates of both the activated sludge and the biofilm, and the nitrogen concentration in the effluent for short (4-10 days) and long (300 days) simulation runs. A calibrated parameter set is proposed (biokinetics, detachment, diffusion) related to the activated sludge, the biofilm and the effluent variables to enhance the model prediction on hourly and daily data sets.
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Affiliation(s)
- Paul Moretti
- Irstea, UR MALY, 5 rue de la Doua, CS 20244, 69625, Villeurbanne Cedex, France
| | - Jean-Marc Choubert
- Irstea, UR MALY, 5 rue de la Doua, CS 20244, 69625, Villeurbanne Cedex, France.
| | - Jean-Pierre Canler
- Irstea, UR MALY, 5 rue de la Doua, CS 20244, 69625, Villeurbanne Cedex, France
| | - Pierre Buffière
- Laboratoire DEEP, Univ Lyon, INSA-Lyon, EA7429, 69621, Villeurbanne, France
| | - Olivier Pétrimaux
- Vinci Environnement France SA, 89 boulevard Franklin-Roosevelt, 92506, Rueil-Malmaison Cedex, France
| | - Paul Lessard
- Département de Génie Civil et de Génie des Eaux, Pavillon Adrien-Pouliot, Université Laval Québec, Québec, Qc, G1V0A6, Canada
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Soliman M, Eldyasti A. Long-term dynamic and pseudo-state modeling of complete partial nitrification process at high nitrogen loading rates in a sequential batch reactor (SBR). Bioresour Technol 2017; 233:382-390. [PMID: 28285231 DOI: 10.1016/j.biortech.2017.02.108] [Citation(s) in RCA: 6] [Impact Index Per Article: 0.9] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 12/16/2016] [Revised: 02/18/2017] [Accepted: 02/22/2017] [Indexed: 06/06/2023]
Abstract
Recently, partial nitrification has been adopted widely either for the nitrite shunt process or intermediate nitrite generation step for the Anammox process. However, partial nitrification has been hindered by the complexity of maintaining stable nitrite accumulation at high nitrogen loading rates (NLR) which affect the feasibility of the process for high nitrogen content wastewater. Thus, the operational data of a lab scale SBR performing complete partial nitrification as a first step of nitrite shunt process at NLRs of 0.3-1.2kg/(m3d) have been used to calibrate and validate a process model developed using BioWin® in order to describe the long-term dynamic behavior of the SBR. Moreover, an identifiability analysis step has been introduced to the calibration protocol to eliminate the needs of the respirometric analysis for SBR models. The calibrated model was able to predict accurately the daily effluent ammonia, nitrate, nitrite, alkalinity concentrations and pH during all different operational conditions.
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Affiliation(s)
- Moomen Soliman
- Department of Civil Engineering, Lassonde School of Engineering, York University, Toronto, Ontario M3J 1P3, Canada
| | - Ahmed Eldyasti
- Department of Civil Engineering, Lassonde School of Engineering, York University, Toronto, Ontario M3J 1P3, Canada.
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