Advanced oxidation processes (AOPs) are commonly used for the destruction of persistent trace organic contaminants (TOrCs) that survive conventional wastewater treatment processes. Three types of AOPs, UV/H2O2, sunlight photolysis and photo-Fenton are experimentally investigated and mathematically quantified to anticipate the fate of TOrCs during oxidation processes, specifically addressing the significant effect of reaction by-products and water matrix on oxidation efficiencies. Hydrogen peroxide UV photolysis is among the most widely used AOPs for the destruction of TOrCs in waters destined for reuse. Previous kinetic models of UV/H2O2 focus on the dynamics of hydroxyl radical production and consumption, as well as the reaction of the target organic with hydroxyl radicals. In this work, we build a predictive kinetic model for the destruction of p-cresol by hydrogen peroxide photolysis based on a complete reaction mechanism that includes reactions of intermediates with hydroxyl radicals. The results show that development of a predictive kinetic model to evaluate process performance requires consideration of the complete reaction mechanism, including reactions of intermediates with hydroxyl radicals. Applying the model to an annular flow-through reactor with reflecting walls, the model mathematically demonstrates that the wall reflectivity significantly enhances the rate of conversion of the target, accounting for the UV light reflection from the reacting walls, as well as the hydrodynamics of the annular flow. Direct and indirect sunlight photolysis is critically important in the breakdown of contaminants in effluent wastewater. The fate of a suite of TOrCs and estrogenic activity were investigated in an effluent-dependent stream. Some TOrCs, which are not sufficiently attenuated through biodegradation and soil adsorption were destructed obviously with distance of travel in the stream. Independent experiments, conducted in batch reactor with 17α-ethinylestradiol (EE2) spiked in effluent showed that attenuation of estrogenic compounds maybe due in part to indirect photolysis caused by formation of reactive species from sunlight absorption. Further investigation was conducted using selective probe compounds to characterize reactive species. And results showed that singlet oxygen generated from excited state of effluent organic matter was responsible for essentially all observed transformations of targets in the effluent in Tucson. To mathematically quantify the photo-Fenton AOP, a kinetic model is proposed for the photolysis of Fe3+ hydroxo complexes at low pH (pH ≤ 3.0). The model incorporates elementary reactions of the Fenton-like and UV/H2O2 system. Iron speciation and photochemical parameters, including the molar absorptivities of light-absorbing species and the quantum yields of Fe3+ and FeOH2+ hydrolysis are experimentally validated. However, the predicted, time-dependent Fe2+ concentrations during Fe3+ photolysis are much lower than measured. The possible missing elements in the model could be (i) quenching of OH radicals by unknown species, or/and (ii) shielding of Fe2+ by unknown compounds at the beginning of the process.

Realized and potential threats of water scarcity due in part to global climate change have increased the interest in potable reuse of municipal wastewater. Recalcitrant trace organic compounds (TOrCs), including pharmaceuticals, steroid hormones and industrial compounds in wastewater are often not efficiently removed by conventional wastewater treatment processes, thereby ubiquitously occurs in natural and wastewater effluents. Advanced water treatment processes including advanced oxidation processes (AOPs), activated carbon adsorption and membrane separation processes have been demonstrated to efficaciously attenuate many classes of TOrCs. In this dissertation, attenuation of TOrCs by ozone oxidation, powdered activated carbon (PAC) and nanofiltration membrane and their monitoring strategies were demonstrated in water reuse applications. Particularly, the first main chapter attempted to elucidate the use of indicator/surrogate for predicting TOrC attenuation by ozone oxidation in a theoretical basis. A semi-empirical model was developed, which successfully predicted many TOrCs with various oxidation kinetics simultaneously. The following chapter was pertaining to development of exploratory models to predict TOrC abatement by ozone. It was concluded that principal component (PC) analysis in conjunction with artificial neural network (ANN) resulted in precise and robust prediction of TOrC attenuation. In addition to oxidation process, kinetic of TOrC adsorption by PAC was scrutinized subsequently. It was found that the initial-phase adsorption was controlled by surface reaction due to hydrophobic interaction. In addition, correlation between surrogate reduction and TOrC attenuation was independent upon water quality at the early phase of adsorption, which was explained theoretically. In the last chapter, synergistic effects of NF membrane in conjunction with pre-ozonation was investigated for TOrC abatement in brine. As a result, all the tested TOrCs were efficaciously attenuated and not quantifiable due to their concentration below limit of quantification. In addition, ozonation also alleviated organic fouling potential substantially.

Although wastewater treatment plants are a line of defense in minimizing indiscriminate output of microconstituents to natural waters, we do not possess a fundamental understanding of the mechanisms involved in microconstituent removal during wastewater treatment. With this in mind, experiments were designed to investigate the factors that can influence the fate of four microconstituents, carbamazepine (CBZ), 17alpha-ethinylestradiol (EE2), iopromide (IOP), and trimethoprim (TMP), during biological suspended culture treatment. Specifically, the role that various ecological members of biological treatment systems play in biotransforming these compounds was evaluated. Sorption assays were performed with inactivated biomass samples (ammonia oxidizing bacteria (AOB), laboratory enriched heterotrophic cultures free of active nitrifiers with low (Ox⁻) or high (Ox⁺) oxygenase activity, and a nitrifying activated sludge (NAS) from a full-scale wastewater treatment plant) to determine whether partitioning dictates removal of individual microconstituents. No microconstituents sorbed to the AOB culture. Neither CBZ nor IOP sorbed to Ox⁻, Ox⁺ and NAS cultures; however, EE2 and TMP sorbed to the Ox⁻, Ox⁺ and NAS biomass. Sorption was positively influenced by the presence of exopolymeric substances (EPS) associated with the cultures. The protein content of EPS affected EE2 and TMP sorption more appreciably than the polysaccharide content of EPS. Further experiments were performed to investigate microconstituent biodegradation by AOBs, Ox⁻ and Ox⁺ cultures. The influence of growth state and oxygenase activity on biotransformation by each culture was also evaluated. Results indicate that EE2 was the only microconstituent that was amenable to biotransformation by batch cultured AOB and heterotrophic cultures. EE2 was biotransformed but not mineralized by AOB chemostat and batch cultures. TMP was not transformed by AOB batch or chemostat cultures; however both EE2 and TMP were transformed by Ox⁻ and Ox⁺ chemostat cultures. Radiolabeled studies showed that EE2 was mineralized by this culture. Kinetically, AOBs dominated EE2 transformation to monohydroxylated metabolites; however, both Ox⁻ and Ox⁺ cultures further degraded and mineralized EE2 and metabolites generated by AOBs. These results indicate that biotransformation of EE2 by NAS may be limited by heterotrophic activity whereas TMP fate may be a function of heterotrophic activity only. Oxygenase activity did not limit EE2 or TMP biotransformation in chemostat cultures. Subsequent experiments that were performed to identify the factors that influence heterotrophic degradation of EE2 and TMP indicated that the presence of readily biodegradable substrates slows EE2 and TMP biotransformation. The impact of slowly biodegradable substrates like EPS on EE2 and TMP degradation was unclear. These results suggest that EE2 and TMP are most amenable to biodegradation in bioreactors where endogenous conditions dominate. / Ph. D.

Nanofiltration (NF) is an attractive option for the treatment of wastewater e.g. municipal wastewater and landfill leachate. However, membrane fouling can be a major obstacle in the implementation of this technology. Fouling of nanofiltration membranes by hu-mic acids (HA) was investigated using bisphenol A (BPA) as an indicator chemical to dif-ferentiate between various mechanisms that may lead to a change in solute rejection. Three commercially available NF membranes were investigated and an accelerated foul-ing condition was achieved with a foulant mixture containing humic acids in an electro-lyte matrix. The effects of membrane fouling on the rejection of BPA were interpreted with respect to the membrane pore sizes and the fouling characteristics. Results report-ed here indicate that calcium concentration in the feed solution could be a major factor governing the humic acid fouling process. Moreover, a critical concentration of calcium in the feed solution was observed, at which membrane fouling was most severe. Mem-brane fouling characteristics were observed by their influence on BPA rejection. Such influence could result in either an increase or decrease in rejection of BPA by the three different membranes depending on the rejection mechanisms involved. It is hypothe-sised that these mechanisms could occur simultaneously and that the effects of each might not be easily distinguished. However, it was observed that their relative contribu-tion was largely dependent upon membrane pore size. Pore blocking, which resulted in a considerable improvement in rejection, was prominent for the more open pore size TFC-SR2 membrane. In contrast, the cake-enhanced concentration polarisation (CECP) effect was more severe for the tighter NF270 and NF90 membranes. For hydrophobic solutes such as BPA, the formation of the fouling layer could also interfere with the so-lute-membrane interaction, and therefore, exert considerable influence on the separa-tion process. The combined impact of humic acid fouling and CaCO3 scaling on the rejection of trace organic contaminants by a commercially available nanofiltration membrane was inves-tigated in this study. Due to the presence of humic acid in the feed solution, CaCO3 scal-ing behaviour differed substantially from that of a pure CaCO3 solution. A prolonged induction period was consistently observed prior to the onset of membrane scaling. In addition, membrane scaling following humic acid fouling did not result in a complete loss of permeate flux. This is consistent with the absence of any large CaCO3 crystals. In fact, the CaCO3 crystals on the membrane surface were quite small and similar in size, which would result in a relatively porous cake layer. At the onset of CaCO3 scaling the rejection of all three trace organic contaminants started to decrease dramatically. The observed decrease in rejection of the trace organic contaminants was much more se-vere than that reported previously with a single layer of either organic or colloidal foul-ing. Such severe decrease in rejection can be attributed to the extended cake-enhanced concentration polarisation effect occurring as a result of the combination of membrane fouling and scaling. The porous CaCO3 scaling layer could lead to a substantial cake-enhanced concentration polarisation effect. In addition, the top CaCO3 scaling layer could reduce the wall shear rate within the underlying humic acid fouling layer, causing an additional concentration polarisation (CP) effect.:1 INTRODUCTION 1 1.1 Fundamentals of NF/RO 1 1.1.1 Solute transport through NF/RO membranes 2 1.1.2 Separation mechanisms 3 1.1.2.1 Steric size exclusion 3 1.1.2.2 Donnan effect 3 1.1.2.3 Electrostatic repulsion 4 1.1.2.4 Adsorption 4 1.1.3 Environmental applications of NF/RO 5 1.1.4 Drinking water treatment from groundwater and surface water sources 5 1.1.5 Water/Wastewater reclamation 7 1.2 Classification and materials of NF/RO membranes 7 1.2.1 Membrane classes 7 1.2.2 Membrane materials 8 1.2.3 Organic membrane materials 9 1.2.3.1 Polyamide membranes 9 1.2.3.2 Cellulose acetate membranes 9 1.2.4 Inorganic membrane materials 10 1.3 Removal of trace organic contaminants 11 1.3.1 Impact of membrane characteristics 14 1.3.1.1 Molecular weight cut-off/pore size 14 1.3.1.2 Surface charge 14 1.3.1.3 Hydrophobicity/hydrophilicity 15 1.3.1.4 Surface morphology 15 1.3.2 Impact of feed characteristics 17 1.3.2.1 pH value 17 1.3.2.2 Ionic strength 18 1.3.2.3 Organic matter 19 1.3.2.4 Presence of divalent ions 20 1.3.2.5 Presence of foulants 20 1.3.2.6 Temperature 20 1.3.3 Impact of solute characteristics 22 1.3.3.1 Molecular weight 22 1.3.3.2 Molecular size (length and width)/molecular volume 22 1.3.3.3 Minimum projection area/Equivalent width 23 1.3.3.4 Charge 23 1.3.3.5 Hydrophobicity/hydrophilicity 24 1.3.4 Impact of operational characteristics 25 1.3.4.1 Transmembrane pressure/permeate or transmembrane flux 25 1.3.4.2 Cross-flow velocity/recovery/concentration polarisation 25 1.3.5 Impact of fouling on rejection 26 1.3.5.1 Organic fouling 28 1.3.5.2 Colloidal fouling 30 1.3.5.3 Inorganic fouling (scaling) 31 1.3.5.4 Biological fouling 32 1.3.6 Impact of membrane cleaning on rejection 32 1.3.6.1 Changes of membrane morphology due to cleaning 32 1.3.6.2 Impact on rejection of TrOCs due to cleaning 33 1.3.7 Validation at pilot and full scale systems 35 2 MEMBRANE FOULING IN THE NANOFILTRATION OF LANDFILL LEACHATE AND ITS IMPACT ON TRACE CONTAMINANT REMOVAL 37 2.1 Introduction 37 2.2 Materials and Methods 40 2.2.1 Analytical reagents and chemicals 40 2.2.2 Nanofiltration membrane 40 2.2.3 Membrane filtration set-up and protocol 41 2.2.4 Analytical technique 42 2.3 Results and discussion 42 2.3.1 Landfill leachate characterisation 42 2.3.2 Physico-chemical properties of bisphenol A 43 2.3.3 Influence of the calcium concentration on the flux 44 2.3.4 Influence of fouling on the rejection of organic contaminants 46 2.4 Conclusions 48 3 CHARACTERISING HUMIC ACID FOULING OF NANOFILTRATION MEMBRANES USING BISPHENOL A AS A MOLECULAR INDICATOR 50 3.1 Introduction 50 3.2 Materials and methods 52 3.2.1 Model NF membranes and membrane characterisation 52 3.2.2 Model trace organic contaminant 52 3.2.3 Organic foulant 53 3.2.4 Membrane filtration set-up 54 3.2.5 Filtration protocol 55 3.2.6 Analytical technique 56 3.3 Results and discussions 56 3.3.1 Membrane characteristics 56 3.3.2 Membrane fouling behaviour 58 3.3.3 Change of membrane hydrophobicity 61 3.3.4 Effects of organic fouling on the nanofiltration of BPA 63 3.3.5 Effects of organic fouling on rejection: the mechanisms 65 3.4 Conclusions 67 4 EFFECTS OF FOULING AND SCALING ON THE REJECTION OF TRACE ORGANIC CONTAMINANTS BY A NANOFILTRATION MEMBRANE: THE ROLE OF CAKE-ENHANCED CONCENTRATION POLARISATION 69 4.1 Introduction 69 4.2 Materials and methods 71 4.2.1 Nanofiltration membrane 71 4.2.2 Chemicals and reagents 71 4.2.3 Crossflow membrane filtration system 72 4.2.4 Experimental protocol 73 4.2.5 SEM-EDS analysis 74 4.2.6 Analytical methods 75 4.3 Results and discussion 75 4.3.1 Membrane characteristics 75 4.3.2 Membrane fouling and scaling development 76 4.3.3 Effects of fouling/scaling on the membrane rejection behaviour 79 4.3.4 Cake-enhanced concentration polarisation 85 4.4 Conclusions 87 5 SUMMARY AND CONCLUSIONS 88 6 REFERENCES 94 7 ACKNOWLEDGEMENTS 112