This study investigated the microbiota in ten different drinking water treatment pools, particles in the Biological Activated Carbon Filtration (BACF) bed, and two mimic columns in the Cheng-Ching Lake Water Treatment Plant. Assimilable organic carbon (AOC) is one of the main nutrition sources for microbes to survive in tap water. Over growing microbes not only decrease the water quality, but also contaminate the water treatment system and distribution system. In this study, we used two molecular biology techniques, the polymerase chain reaction (PCR) and denaturing gradient gel electrophoresis (DGGE), to analyze the dynamic microbial communities and biodiversities in the drinking water cleaning system and the micorbiota that exist in the BAC and anthracite filtration pellets. The bacterial 16S rDNA sequences resulted from PCR-DGGE were compared with the data in the Ribosomal Database Project Bank to construct a phylogenetic tree which allowed us to understand the microbial communities and biodiversities in the drinking water treatment pools and the filtration pellets. The total bacterial count and PCR-DGGE profiles showed that the drinking water quality had been improved during the treating processes and most of the microbes in raw water were removed. The scanning electron microscopy clearly indicated the biofilms were developed on the pellet surface. From the mimic column studies, the PCR-DGGE profiles suggested that various microbial communities were present on different depth of the columns samples. In comparing the 16S rDNA sequences with Gene Bank, many are new category bacteria were found and most of them are unculturable. Most of these microbes belong to the beta-proteobacterium. Although many bacteria were located on the surface of the filtration pellet, the BAC and anthracite could still absorb AOC efficiently to enhance the bacteria growth. The over growing bacteria might release out and contaminate the drinking water. Therefore, we suggest that it is important to backwash the filter bed frequently in order to diminish microbes of the filtration pellet and avoid re-contaminate the drinking water.

The presence of micropollutants, particularly pesticides, in surface waters across Canada has been of concern not only for their environmental impact, but also for their potential effects on human health and recalcitrant nature to conventional water treatment methods. Although ozone has been mainly applied for disinfection of drinking water, oxidation of trace organics by ozonation has been considered potentially effective. In an effort to meet increasingly stringent drinking water regulations, different solid catalysts have been used to enhance the removal of water contaminants by ozonation. In spite of the increasing number of data demonstrating the effectiveness of heterogeneous catalytic ozonation, the influence of different factors on the efficiency of micropollutants oxidation is still unclear.<p> In the present work, application of three solid catalysts in ozonation of two model micropollutants in pure water was examined using a laboratory-scale reaction system over a range of operating conditions. The three catalysts investigated were activated carbon, alumina, and perfluorooctyl alumina, and the two model micropollutants were the pesticides atrazine and 2,4-dichlorophenoxyactic acid. The effects of solution pH, presence of a radical scavenger, pesticide adsorption on catalyst, and catalyst dose on micropollutant removal were investigated. Solution pH was found to significantly influence the catalyst ability to decompose ozone into free hydroxyl radicals. The effect of these free radicals was markedly inhibited by the radical scavenger resulting in a negative impact on pesticides degradation. In general, the removal rate of pesticides was found to increase with increasing doses of catalyst.<p> In the ozonation process in the presence of activated carbon, atrazine removal rates increased four and two times when using a catalyst dose of 0.5 g L-1 at pH 3 and 7, respectively, whereas observed reaction rates for 2,4-D increased over 5 times in the presence of 1 × 10-4 M tert-butyl alcohol at pH 3. In the ozonation system catalyzed by 8 g L-1 alumina, the observed reaction rate constant of atrazine removal notably improved at neutral pH by doubling the micropollutant removal rate. For the pesticide 2,4-D in the presence of 1 × 10-4 M tert-butyl alcohol at pH 5, the observed removal rate was over ten times higher than that for the non-catalytic ozonation process using also using a catalyst dose of 8 g L-1. Modification of alumina to produce perfluorooctyl alumina resulted in a material able to significantly adsorb atrazine, while not exhibiting affinity for adsorption of 2,4-D. In spite of its adsorptive properties, perfluorooctyl alumina was found to enhance neither molecular ozone reactions nor ozone decomposition into hydroxyl radicals. Thus, the observed removal rates for atrazine and 2,4-D by ozonation in the presence of perfluorooctyl alumina did not increase significantly.

Solar water disinfection (SODIS) is the process of treating microbiologically contaminated water in clear plastic bottles through exposure to sunlight. One of the major limiting factors of this treatment is source water quality. This work investigates the impact of organic matter and turbidity on SODIS efficiency. Organic matter was found to decrease bacterial inactivation to a much greater extent than the presence of inorganic particles. The ability of moringa oleifera seed emulsion to clarify source waters was investigated as a coagulation pretreatment. This coagulant is most effective in highly turbid, high humic content waters, and achieves up to 1-log bacterial removal. The combined moringa oleifera coagulation-SODIS treatment sequence was tested in highly coloured natural source water and was found to reduce the sunlight exposure time required by up to 2 hours. Treated water should be consumed immediately following the individual or combined treatments due to the potential for bacterial regrowth.

To improve biogas production from lignocellulosics, methanogenic microbial enrichments were prepared from moose rumen fluid, beaver droppings, and internal circulation (IC) reactor granules amended with cellulose, pine needles, lignosulphonate, tannic acid, and poplar hydrolysate. Tannic acid delayed methanogenesis compared to cellulose only enrichments, both by reducing initial rates (up to 50% in beaver dropping cultures) and increasing lag times (up to 50 days in moose rumen cultures). Biogas yields from poplar hydrolysate were 56 % by beaver droppings, 51% % by IC granules, and 31 % by moose rumen enrichments. Bacterial community profiles, determined via denaturing gradient gel electrophoresis (DGGE) showed divergent populations between enrichments. Enrichment on pine needles or poplar hydrolysate promoted bioconversion of post extraction wash (PEW), and beaver dropping enrichments fed pine needles equaled the yield (about 23%) from IC granules. Together, the DGGE and PEW results provide evidence of acclimatization to previously recalcitrant feeds.

Previous research indicates that pharmaceutically active compounds (PhACs) and endocrine-disrupting compounds (EDCs) are poorly removed during conventional drinking water treatment processes including coagulation; however, removal efficiency increases in the presence of natural organic matter (NOM). Therefore, this project investigates the link between various NOM types with EDC/PhAC removal. Bench-scale coagulation tests were conducted on three different source waters spiked with environmentally relevant levels (nominally 1000 ng/L) of EDCs/PhACs. Two different coagulants were used: polyaluminum chloride (PACl) and aluminum sulphate (alum). NOM was characterized using size exclusion liquid chromatography-organic carbon detection (LC-OCD). Results for Lake Ontario, Otonabee and Grand River water indicate that certain EDCs/PhACs are significantly removed during coagulation while others increase in concentration. Concurrently, particular NOM fractions (biopolymers and humic substances) are also being removed. Solvents used for EDC/PhAC spiking (acetone and acetonitrile) did not affect coagulation, but contributed to low molecular weight neutral and hydrophobic NOM fractions.

Solar water disinfection (SODIS) is the process of treating microbiologically contaminated water in clear plastic bottles through exposure to sunlight. One of the major limiting factors of this treatment is source water quality. This work investigates the impact of organic matter and turbidity on SODIS efficiency. Organic matter was found to decrease bacterial inactivation to a much greater extent than the presence of inorganic particles. The ability of moringa oleifera seed emulsion to clarify source waters was investigated as a coagulation pretreatment. This coagulant is most effective in highly turbid, high humic content waters, and achieves up to 1-log bacterial removal. The combined moringa oleifera coagulation-SODIS treatment sequence was tested in highly coloured natural source water and was found to reduce the sunlight exposure time required by up to 2 hours. Treated water should be consumed immediately following the individual or combined treatments due to the potential for bacterial regrowth.

To improve biogas production from lignocellulosics, methanogenic microbial enrichments were prepared from moose rumen fluid, beaver droppings, and internal circulation (IC) reactor granules amended with cellulose, pine needles, lignosulphonate, tannic acid, and poplar hydrolysate. Tannic acid delayed methanogenesis compared to cellulose only enrichments, both by reducing initial rates (up to 50% in beaver dropping cultures) and increasing lag times (up to 50 days in moose rumen cultures). Biogas yields from poplar hydrolysate were 56 % by beaver droppings, 51% % by IC granules, and 31 % by moose rumen enrichments. Bacterial community profiles, determined via denaturing gradient gel electrophoresis (DGGE) showed divergent populations between enrichments. Enrichment on pine needles or poplar hydrolysate promoted bioconversion of post extraction wash (PEW), and beaver dropping enrichments fed pine needles equaled the yield (about 23%) from IC granules. Together, the DGGE and PEW results provide evidence of acclimatization to previously recalcitrant feeds.

Previous research indicates that pharmaceutically active compounds (PhACs) and endocrine-disrupting compounds (EDCs) are poorly removed during conventional drinking water treatment processes including coagulation; however, removal efficiency increases in the presence of natural organic matter (NOM). Therefore, this project investigates the link between various NOM types with EDC/PhAC removal. Bench-scale coagulation tests were conducted on three different source waters spiked with environmentally relevant levels (nominally 1000 ng/L) of EDCs/PhACs. Two different coagulants were used: polyaluminum chloride (PACl) and aluminum sulphate (alum). NOM was characterized using size exclusion liquid chromatography-organic carbon detection (LC-OCD). Results for Lake Ontario, Otonabee and Grand River water indicate that certain EDCs/PhACs are significantly removed during coagulation while others increase in concentration. Concurrently, particular NOM fractions (biopolymers and humic substances) are also being removed. Solvents used for EDC/PhAC spiking (acetone and acetonitrile) did not affect coagulation, but contributed to low molecular weight neutral and hydrophobic NOM fractions.

Nowadays, organic pollutants occurring in surface waters have raised substantial concern in public. Triclosan (TCS) is one of the antimicrobial agents which are utilized in both domestic and industrial application. In this study nanofiltration (NF) of TCS in surface water was investigated. Laboratory scale cross-flow device is operated in total recycle mode and DK-NF and DL-NF membranes were used. Kesikk&ouml / pr&uuml / Reservoir (Ankara) water was used as raw water. Effect of natural organic matter (NOM) content of raw water on TCS removal is searched through addition of humic acid (HA) into the raw water as to represent for NOM. Steady state permeate fluxes are monitored throughout the experiments to explore the flux behavior of the membranes. During the experiments, performance of the membranes is assessed by monitoring TCS, as well as other water quality parameters, such as UVA254 and total organic carbon (TOC) in the feed and permeates waters. Results obtained put forward that TCS removal by NF membrane is not as same as reported in the literature. In the literature, membrane removal efficiency is reported as above 90%. However, this study proved that this would be true if and only if one does not considers the adsorption of TCS by the system itself, in the absence of membrane. It is now clear that, because of adsorption of the TCS onto the experimental set up (feed tank, pipings etc.) / the real TCS removal efficiency of the nanofiltration is around 60-70%.

A series of pilot-scale granular media filtration experiments was conducted to examine the effect of media roughness on filter performance and to evaluate the applicability of spherical, rough engineered ceramic filter media for use in granular media filters used for drinking water treatment. Filter media performance was assessed using turbidity and particle count reductions, Cryptosporidium oocyst and oocyst-sized microsphere removal, head loss and stability of operation. Experiments were designed to allow related facets of current filtration research to be examined. These included: effect of loading rate, coagulant type and dosage, and suitability of latex microspheres as surrogates for Cryptosporidium oocyst removal by granular media filtration. This study indicated that increased filter media roughness consistently improved turbidity and particle count reduction under the conditions investigated. As well, the engineered media also consistently achieved greater stability of operation during non-ideal operational periods (e.g. sudden change in filter influent turbidity).Oocyst removals were generally improved by media roughness, though this improvement was reliant on operating conditions, such as coagulant dose and type of coagulant used. The surrogate relationship between oocyst-sized latex microspheres and oocyst removal by filtration was also dependent on coagulant dose and type of coagulant. During trials with no coagulant addition, contrasts in oocyst removal were not significant, suggesting that neither surface roughness nor the size of media used were significant factors impacting oocyst removal by filtration during those periods of impaired operation. When pre-treating raw water with PACl, the engineered ceramic media achieved up to 1.25 log10 higher oocyst removals than conventional media. This improvement in oocyst removal relative to conventional media was not observed when alum was used as the primary coagulant, however. Future studies should directly compare engineered and conventional media filtration performance, using other raw water sources and different operating conditions. Biologically active filtration should also be included in future performance studies because the rough, highly porous surface of the engineered ceramic media is likely to provide excellent biofilm support.