There is an urgent need to develop ammonia removal treatment systems for municipal and industrial wastewater treatment due to the increasingly stringent ammonia effluent discharge regulations implemented by Canada, the United States, and the European Union. The objective of this dissertation is to develop new understanding and advance the current design and operation of total ammonia nitrogen (TAN) removal via the moving bed biofilm reactor technology (MBBR) for municipal and industrial wastewaters. The first specific objective is to develop a passive, low operationally intensive, efficient and robust design strategy for municipal wastewater treatment to achieve partial nitritation (PN) as a pre-treatment to anammox treatment without using control strategies such as operating at low dissolved oxygen, or the use of inhibitors. This first objective includes developing new knowledge of the biofilm, biomass and microbiome of attached growth PN systems. The second specific objective is to investigate the impact of defining a maximum biofilm thickness, via bio-carrier design, to enhance the effects of free nitrous acid inhibition for PN of municipal wastewaters. The third objective is to investigate the effect of influent copper concentration on nitrifying MBBR systems over long-term operations, to demonstrate the feasibility of the nitrifying MBBR as a solution for TAN removal from gold mining wastewaters. The results pertaining to the first objective, achieved via a study investigating the operation of a nitrifying moving bed biofilm reactor at elevated TAN surface area loading rates (SALRs) of 3, 4, 5, and 6.5 g TAN/m²∙d with the aim of achieving passive PN, demonstrates that operating at a TAN SALR value of 6.5 g TAN/m²∙d can achieve PN without restricting dissolved oxygen or using inhibitors. Operating at a TAN SALR value of 6.5 g TAN/m²∙d achieves a TAN surface area removal rate (SARR) of 3.5 g TAN/m²∙d, and a nitrite accumulation of 99.8% of the oxidized TAN, demonstrating the suppression of nitrite oxidizing bacteria (NOB) activity, while achieving elevated TAN SARR values. At the molecular-scale, there is a statistically significant change in the ammonia oxidizing bacteria (AOB) to NOB ratio from 1:2.6 to 8.7:1 as the TAN SALR increases from 3 to 6.5 g TAN/m²∙d; however, even at a TAN SALR value of 6.5 g TAN/m²∙d there is an NOB abundance of approximately 2%; thus demonstrating that NOB remain present in the biofilm, while their activity is suppressed by operation at elevated TAN SALR values. Furthermore, this system was shown to achieve stable PN consistently for over a period of 10 months of operation, demonstrating a robust, passive, low operational strategy for attached growth PN. The second objective of this dissertation is addressed through a study that compared the carrier design of defined maximal biofilm thickness (z-prototype carrier) to undefined maximal biofilm thickness (chip-prototype carrier) for PN via free nitrous acid inhibition of tertiary, low carbon, municipal wastewaters. The study demonstrates that defined maximal biofilm thickness is a preferred design choice to achieve attached growth PN. The chip-prototype carrier shows biofilm thicknesses and biofilm mass values that are ten-fold higher than the z-prototype carrier, which is shown to contribute to the impact of free nitrous acid on AOB and NOB activities. The z-prototype carrier shows PN is achieved after 3 hours of exposure to free nitrous acid while the chip-prototype carrier does not achieve PN within this same time of exposure. Therefore, the defined maximal biofilm thickness carrier is identified in this research as the preferred design option to achieve attached growth PN for municipal, low carbon, tertiary wastewater treatment. The results of the third objective, achieved via a study investigating the effects of influent copper concentrations on nitrifying MBBR during long term operations to gold mining wastewaters, demonstrates that there is no AOB inhibition in attached growth systems exposed to 0.1, 0.3, 0.45, and 0.6 mg Cu/L for long exposure times. A trend of increasing nitrite accumulation with increasing influent copper concentrations is shown, indicating that NOB inhibition occurs at influent copper concentrations of 0.3 mg Cu/L and greater, with the greatest NOB inhibition observed with an influent copper concentration of 0.6 mg/L. There is no statistically significant difference in biofilm characteristics at the copper concentrations tested; however, there is a trend of increasing biofilm thickness and biofilm roughness with increasing copper concentrations. This study demonstrates the resilience of the nitrifying biofilm to copper inhibition and demonstrates that the nitrifying MBBR is a promising system for removing TAN in mining wastewater in the presence of copper.

Occurrence of organic micropollutants (OMPs) in aquatic environment is a worldwide concern. A long list of anthropogenic substances, including pharmaceuticals, hormones, etc., are frequently detected in natural water sources. Wastewater treatment plants are one main source of OMPs pollution, but also a key step to control OMPs dissemination into the environment. This dissertation focuses on the evaluation of Membrane Aerated Biofilm Reactor (MABR) as a sustainable process to treat wastewater polluted by OMPs. Furthermore, application of high intensity pulsed light is proposed as an innovative tertiary treatment to produce reclaimed water of high quality. In Chapter 1, a literature review was performed to investigate the occurrence and toxicity of 12 selected organic micropollutants (OMPs) in surface and ground water and the limitations of current available biological processes. Among these technologies, systems with enriched nitrifying activity were able to enhance the removal of specific OMPs through cometabolic activities. Thus, I proposed the use of a MABR with enriched nitrifying biomass to treat OMP polluted water. In Chapter 2, I studied the influence of biofilm thickness on the removal of 13 OMPs via MABR. Results demonstrated OMP removal was dependent on biofilm thickness and bacterial cell density. MABR demonstrated important efficiencies in the removal of ammonium, COD, acetaminophen and triclosan at early stages of biofilm thickness. However, the removal of nonpolar, hydrophobic 4 OMPs and anionic, acidic OMPs required thicker biofilms, achieving maximum removal at biofilm with 1.02 mm thickness and 2.2 × 106 cell mL-1. In Chapter 3, the contribution of sorption and biodegradation in the removal of OMPs via MABR was evaluated. At three stages of biofilm thickness studied, biodegradation dominated the removal for most OMPs. Heterotrophs played an important role in OMP biodegradation at all biofilm thickness, while autotrophic nitrifiers enhanced their contribution at thickness beyond 0.58 mm. Increased removal of pollutants like estrone and ethinyl estradiol were linked to the MABR enrichment with nitrifying bacteria. Sorption was essential for the removal of lipophilic and recalcitrant pollutants like triclosan. Finally, to provide high quality treated water for reuse, Chapter 4 explores the use of high-intensity pulsed light (HIPL) as post-treatment. The number of pulses and optical energy dose have a significant impact on the OMPs removal. HIPL demonstrated fast kinetics and efficient photodegradation – with significant OMPs removal within milliseconds. The findings from my Ph.D. dissertation indicate that MABR combined with high-intensity pulse light may be an effective treatment train for the efficient removal OMPs present in municipal wastewaters. This combined treatment process could potentially pave the way to produce high quality reclaimed water for various reuse purposes.