Abstract

Researchers have observed that the biofilm nitrification rate (NR) in membrane-aerated biofilm reactor (MABR) systems did not deteriorate at low winter temperatures. Using the pilot data, the temperature impacts were studied in two different approaches. A close-to-unity temperature coefficient (θ=1.007) and a constant half-velocity constant (KN,BF=5.7  mgN/L) were obtained from the semiempirical kinetic-based approach, indicating that the bulk NH4+-N concentration, rather than temperature, was determining the biofilm NR. The pilot performance was also simulated in GPS-X 7.0 using all typical kinetic values from scientific literatures except the hydrolysis rate constant. A lower hydrolysis rate constant (0.15  day1) was used to match the data during calibration and it should be considered as a lumped effect of the pilot conditions. While the temperature effects on biological kinetics are well established, they were masked by the dynamic changes in the MABR biofilm. The apparently weak impact of temperature on the biofilm NR distinguishes the MABR technology as a novel solution for nitrification intensification. The two simulation approaches are proved effective as tools for the process design.

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Data Availability Statement

Some or all data, models, or code generated or used during the study are available from the corresponding author by request.
1.
Chicago demo process data June 15 final_2016. Xlsx: this is the pilot data and data analysis;
2.
Chicago demo GPS-X Part 1: this is the simulation of the pilot when the number of membrane modules is 64 (the number of modules cannot be dynamically simulated; therefore, the simulation of pilot was divided into two simulation periods, one for 64 modules and the other for 48 modules);
3.
Chicago demo GPS-X Part 2: this is the simulation of the pilot when the number of modules is 48;
4.
simulation data analysis.xlsx: this file contains the simulation results from Files 2 and 3, data analysis and most figures;
5.
batteryDfeedfinal.xlsx: this is the feed to Battery D of O’Brien WRP and main operational conditions of this battery during the simulation period and was mainly obtained from the plant data file with some parameters estimated for simulation purposes; and
6.
Chicago demo GPS-X input.xlsx: this file contains all the simulation results of Battery D and all other inputs from the pilot, which serves as the input for the pilot simulation, and was split into two data files, which were used for the pilot simulation in Files 2 and 3.

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Go to Journal of Environmental Engineering
Journal of Environmental Engineering
Volume 146Issue 6June 2020

History

Received: Feb 7, 2019
Accepted: Dec 3, 2019
Published online: Apr 6, 2020
Published in print: Jun 1, 2020
Discussion open until: Sep 6, 2020

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Senior Research Engineer, SUEZ Water Technologies & Solutions, 3239 Dundas St. West, Oakville, ON, Canada L6M 4B2 (corresponding author). ORCID: https://orcid.org/0000-0002-0825-8474. Email: [email protected]
Ali K. Oskouie, Ph.D. [email protected]
Senior Research Scientist, Metropolitan Water Reclamation District of Greater Chicago, 6001 West Pershing Rd., Cicero, IL 60804; Adjunct Professor, Dept. of Civil, Architectural and Environmental Engineering, Illinois Institute of Technology, Chicago, IL 60616. Email: [email protected]
Thomas E. Kunetz [email protected]
Assistant Director of Monitoring and Research, Metropolitan Water Reclamation District of Greater Chicago, 100 East Erie St., Chicago, IL 60611. Email: [email protected]
Jeff Peeters [email protected]
Product Manager, SUEZ Water Technologies & Solutions, 3239 Dundas St. West, Oakville, ON, Canada L6M 4B2. Email: [email protected]
Technology Manager, SUEZ Water Technologies & Solutions, 3239 Dundas St. West, Oakville, ON, Canada L6M 4B2. ORCID: https://orcid.org/0000-0002-4579-0099. Email: [email protected]
Dwight Houweling, Ph.D. [email protected]
Senior Research Engineer, SUEZ Water Technologies & Solutions, 3239 Dundas St. West, Oakville, ON, Canada L6M 4B2. Email: [email protected]

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