This thesis reports on research from a full-scale demonstration project to recharge a depleted aquifer with treated sewage effluent from the Paphos (Cyprus) wastewater treatment plant. The project artificially recharged the Ezousas river basin, located in the south-western coastal plain of Cyprus, with tertiary treated, disinfected effluent through a network of artificial infiltration ponds. The aims of the research were to determine the capacity of the aquifer to provide a suitable buffer for the flow from the wastewater without flooding and to measure the changes in reclaimed water quality. The aquifer hydraulics and treatment capacity, including recharge basins, were analysed using field and laboratory measurements. A geological field survey and modelling was used to assess, both by practice and theory the effectiveness of the Ezousas river aquifer for storage and recovery of the reclaimed water. The aquifer was found to be mainly composed of alluvium with typical hydraulic characteristics. The average porosity was 20% and hydraulic conductivity around 90 m/day, it was concluded the aquifer would be able to accept all the annual output of the treatment plant which was 5 Mm3 /a. The recharge network consisted of five groups of infiltration basins arranged on both banks of the River Ezousas about 2km upstream of the wastewater treatment plant. Each infiltration basin contained two, four or six recharge ponds, each basin was 2,000m2 in area with a depth of 1.5 m. A recharge pattern consisting of alternating weeks of wet-fill and drying cycles was found necessary to maintain the unsaturated zone below the ponds in order to maximise the amount of water that could be recharged whilst optimising water quality. The hydraulic impact of the artificial recharge and extraction from the field measurements of borehole water levels indicated recharged water down to 15m below the surface. Tracer tests on the groundwater flow, capture zone, residence times and mass balances of recharged and native waters gave widely varying residence times between 30 days and 5 years, these were attributed to the complex flow patterns found. Recharged water was sampled using a series of extraction wells located along the downstream river basin, starting at the infiltration ponds and then at stages downstream. Eight production and monitoring wells were tested including control samples up-gradient (upstream) from the ponds, to about 7km down-gradient (downstream). Water quality was analyzed for the standard wastewater constituents including indicator organisms, organic matter, nutrients N and P and the metals. It was one of the recommendations of the thesis however that attention also be paid to the persistent organics, including the pesticides, biocides, plasticizers and pharma residues. The chemical data was used to build and validate a solute transport model of the ponds and surrounding area to predict the transport and fate of priority contaminants. In this way, the geo-chemical potential for the retardation, attenuation and chemical or biochemical degradation processes taking place in the unsaturated and saturated zone were assessed. From the results it was concluded that for most analytes, which included metals, nitrate and common salts, the main processes were mixing and dilution by the native ground water. The extracted water was then a mix of waters according to the different residence times and flow of natural groundwater, giving a stable water quality for irrigation. A third reaction involving cation exchange with the local geology was however identified which reduced the concentrations of copper and phosphate beyond what was expected from just mixing. It was also concluded that denitrification did not occur because of a combination of the high quality of the effluent, the operational cycling of the ponds and the high porosity of the vadose zone. Previous work has found denitrification if the recycled water still contains organic matter, further work was recommended to determine the critical organic concentrations. The renovated water from the Ezousas wastewater reuse Project was able to meet the health and agronomic requirements for unrestricted irrigation. The risk of flooding with sewage effluent resulting from hydraulic mounding was also investigated to define the growth and decay of the mound. It was possible to report that after more than fifteen years of operation and a total infiltration of 40Mm3, there have been no signs of reduced hydraulic capacity or water quality.

L’anthropisation médicamenteuse des eaux usées favorise l’émergence et la diffusion dans l’environnement de microorganismes résistants aux antibiotiques. Les effluents hospitaliers pourraient être doublement impliqués en véhiculant antibiotiques et bactéries multirésistantes. L’objectif de ce travail est de caractériser les effluents hospitaliers d’un Centre Hospitalo-Universitaire en évaluant simultanément les concentrations d’antibiotiques (fluoroquinolones et imipénème) et la diversité des bactéries résistantes à ces antibiotiques au sein de biofilms constitués in situ. Les concentrations en antibiotiques mesurées par chromatographie en phase liquide - spectrométrie de masse après collecte via un échantillonnage passif pendant 15 jours sont égales à 2,08±0,88μg/L (ciprofloxacine), 101,06±18.47 μg/L (ofloxacine), 6,43±0.56 μg/L (norfloxacine) et indétectable pour l’imipénème. Comparées aux données de consommation à l’hôpital pendant cette même période, les concentrations estimées sont 5,84±1,78μg/L (ciprofloxacine), 11.22±1.09μg/L (ofloxacine), 7.68±3,7μg/L (norfloxacine) et 3,61±0,24ug/L (imipénème). La mesure du risque potentiel écotoxicologique s’est avérée positive pour la ciprofloxacine et la norfloxacine (hazard quotient >1). En parallèle, des bactéries résistantes aux fluoroquinolones (n=115) ou aux carbapénèmes (n=38) ont été isolées de biofilms formés dans les effluents hospitaliers. 60 % des isolats, constitués majoritairement de bacilles à Gram négatif, notamment Aeromonas spp et Klebsiella spp, sont résistants à plusieurs familles d’antibiotiques dont certains sont exclusivement utilisés à l’hôpital. La majorité des souches hébergent des éléments génétiques mobiles dont des plasmides conjugatifs porteurs de la résistance à l’imipénème ou aux fluoroquinolones. La présence combinée de bactéries résistantes aux antibiotiques hébergeant des éléments génétiques mobiles en lien avec ces résistances et de faibles concentrations en antibiotiques permet de qualifier l’interface hôpital-environnement comme un lieu propice au transfert des résistances. / The presence of pharmaceutical compounds in waste water favors the emergence and the spreading of antibiotic resistant microorganisms. The hospital effluents could be involved gathering antibiotics and multiresistant bacteria. The aim of this work is to characterize the hospital effluents of a teaching hospital measuring simultaneously the concentrations of antibiotics (fluoroquinolones and imipenem) and the diversity of the bacteria resistant to these antibiotics within hospital effluent biofilms.The antibiotics concentrations were measured by liquid-phase chromatography - mass spectrometry via a passive sampling during 15 days. The measured environmental concentrations were 2.08 ± 0.88μg/L (ciprofloxacin), 101.06 ± 18.47 μg/L (ofloxacine), 6.43 ± 0.56 μg/L (norfloxacine). Imipenem was not detected. Compared with the data of hospital consumption during the same period, the predicted estimated concentrations are 5.84±1.78µg/L(ciprofloxacin), 11.22 ± 1.09µg/L (ofloxacin), 7.68 ± 3.7µg/L, 7.68 ± 3.7μg/L (norfloxacin) and 3.61 ± 0.24ug/L (imipenem). The ecotoxicological risk was confirmed for the ciprofloxacin and the ofloxacin (hazard quotient > 1).In parallel, fluoroquinolones (n=115) and carbapenem (n=38) resistant bacteria were isolated from hospital effluent biofilm. Sixty % of isolates, mainly composed by Gram negative bacilli in particular Aeromona spp and Klebsiella spp, are resistant to several antibiotics among which some are exclusively used at the hospital. The majority of these strains have mobile genetic elements such as conjugative plasmids harboring imipenem or fluoroquinolones resistances.The presences of both antibiotics resistant bacteria harboring mobile genetic elements in connection with these resistances and low antibiotics concentrations make the hospital effluent a convenient place for the transfer of resistance between the hospital and the environment.

The presence of human pharmaceuticals in the aquatic environment is now becoming a well-established fact. The identified problems associated with their presence include the fact that these compounds are biologically active, some of them are toxic in nature, and a number of compounds have potential to foster and maintain drug resistant microorganisms. They are discharged into the aquatic environment from a variety of sources, but mainly by the excretion of incompletely metabolized pharmaceuticals by individuals into the wastewater. This situation makes finding a source-control strategy difficult. However, healthcare facility (hospitals and long-term-care homes) effluents are suspected to have relatively higher concentrations of these compounds, as such facilities use pharmaceuticals in large amounts for diagnostic, cure and research purposes. It is expected that controlling discharges from these facilities may provide a cost-effective solution to reduce the pharmaceutical loads entering the aquatic environment.

Treated wastewater (effluent) has been used as a water source for aquifer recharge and sustaining perennial surface water flow. Artificial recharge basins allow effluent to seep into the ground relieving stressed aquifers. However, these basins frequently become clogged due to physical, chemical, and biological processes. Effluent is also used to replace baseflow for dry streambeds. However, little is known about the effect of effluent on stream-aquifer interactions. Effluent from the Nogales International Waste Water Treatment Plant sustains perennial flow in the Upper Santa Cruz River, Arizona. A series of monthly field campaigns were undertaken to understand the impact of effluent on the streambed at 16 different sites along a 30 km river reach. The field campaigns had two foci: physical transformations in the streambed and water source identification using chemical composition. Historic data sets including USGS stream gauging records, NIWTP outfall data, ADWR well transducer data and USGS well chemistry data were also analyzed to provide a larger context for the work. Results indicate that localized clogging forms in the Upper Santa Cruz River. The clogging layers perch the stream and shallow streambed causing a desaturation below the streambed. A clogging cycle is established in the context of a semi-arid hydrologic cycle: formation during dry and hot pre-monsoon months, and removal by a set of large flood flows (10+ m3/sec) during the monsoon season. However, if the intensity of flooding during the semi-arid hydrologic cycle is lessened, the dependent riparian area can experience a die off.

The presence of human pharmaceuticals in the aquatic environment is now becoming a well-established fact. The identified problems associated with their presence include the fact that these compounds are biologically active, some of them are toxic in nature, and a number of compounds have potential to foster and maintain drug resistant microorganisms. They are discharged into the aquatic environment from a variety of sources, but mainly by the excretion of incompletely metabolized pharmaceuticals by individuals into the wastewater. This situation makes finding a source-control strategy difficult. However, healthcare facility (hospitals and long-term-care homes) effluents are suspected to have relatively higher concentrations of these compounds, as such facilities use pharmaceuticals in large amounts for diagnostic, cure and research purposes. It is expected that controlling discharges from these facilities may provide a cost-effective solution to reduce the pharmaceutical loads entering the aquatic environment.

The research project was formulated to solve serious environmental and possible public health problems in rural and regional areas caused by the common failure of soil disposal systems used for application of effluent from on-site domestic sewage treatment systems. On-site sewage treatment systems adopt a treatment train approach with the associated soil disposal area playing a crucial role. The most common on-site sewage treatment system that is used is the conventional septic tank and subsurface effluent disposal system. The subsurface effluent disposal area is given high priority by regulatory authorities due to the significant environmental and public health impacts that can result from their failure. There is generally very poor householder maintenance of the treatment system and this is compounded by the failure of the effluent disposal area resulting in unacceptable surface and groundwater contamination. This underlies the vital importance of employing reliable science-based site suitability assessment techniques for effluent disposal. The research undertaken investigated the role of soil physico-chemical characteristics influencing the behaviour of effluent disposal areas. The study was conducted within the Logan City Council area, Queensland State, Australia. About 50% of the Logan region is unsewered and the common type of on-site sewage treatment used is a septic tank with subsurface effluent disposal area. The work undertaken consisted of extensive field investigations, soil sampling and testing, laboratory studies and extensive data analysis. In the field study, forty-eight sites were investigated for their effluent application suitability. The sites were evaluated based on the soil physico-chemical characteristics. The field investigation indicated that there were nine soil orders in the study area. These soil orders were Dermosols, Chromosols, Kandosols, Kurosols, Vertosols, Sodosols, Tenosols, Rudosols and Anthrosols. The soils in all the investigated sites were acidic soils in the pH range between 5 and 6.5. The complexity of the large data matrix obtained from the analysis was overcome by multivariate analytical methods to assist in evaluating the soils' ability to treat effluent and to understand the importance of various parameters. The analytical methods selected to serve this purpose were PROMETHEE and GAIA. The analysis indicated that the most suitable soils for effluent renovation are the Kandosols whilst the most unsatisfactory soil order was found to be Podosol. The GAIA analysis was in agreement with quantitative analysis conducted earlier. An extensive laboratory column study lasting almost one year was undertaken to validate the results of the data analysis from the field investigation. The main objectives of this experiment were to examine the soil behaviour under practical effluent application and to investigate the long-term acceptance rate for these soils. Twelve representative soils were selected for the column experiment from the previously investigated sites and undisturbed soil cores were collected for this purpose. The results from the column study matched closely with the evaluation conducted at the earlier stages of the research. Soil physico-chemical analysis before and after effluent application indicated that the soils' acidity was improved toward neutrality after effluent application. The results indicated that soils have a greater ability to handle phosphorus than nitrogen. The most favorable cation exchange capacity for soils to treat and transmit effluent was between 15 and 40 meq/100g. Based on the results of the column study, the long-term acceptance rate (LTAR) was determined for the investigated twelve soil types. Eleven out of twelve soils reported specific LTAR values between 0.18-0.22 cm/day. For the duration of the laboratory study, the Podosol order did not reach its LTAR value due to the extremely sandy nature of the soil. The time required to achieve LTAR varied between different soils from 40 to 330 days. The outcomes of this research was integrated into a soil suitability map for on-site sewage treatment systems for Logan City Council. This will assist the authorities in providing sustainable solutions for on-site systems failure.

O presente trabalho foi realizado em sua maior parte no Brasil. Entretanto, com o intuito de enriquecer a pesquisa, realizou-se coleta de dados por um período de seis meses na Universidade de Wageningen - Holanda. Na etapa realizada no Brasil se propôs: estudar a formação de subprodutos (aldeídos e trialometanos) da desinfecção de efluente de tratamento anaeróbio esgoto sanitário com ozônio, cloro e ozônio/cloro; verificar como os desinfetantes atuam no processo de oxidação; conhecer o grau de toxicidade bem como o efeito do residual do ozônio e cloro empregando Daphnia similis e Danio rerio como organismos-teste e, ainda, analisar a eficiência do ozônio, cloro, ozônio/cloro na inativação de microrganismos. Na etapa da pesquisa realizada na Holanda se propôs: estudar a formação de subprodutos (aldeídos) da desinfecção de efluente de tratamento anóxico com ozônio, ozônio/cloro e ozônio/peróxido de hidrogênio (peroxônio); verificar como os desinfetantes atuam no processo de oxidação; e, ainda, analisar a eficiência do ozônio, ozônio/cloro na inativação de microrganismos indicadores. Nos estudos realizados, pode-se verificar uma expressiva formação de aldeídos com predominância de formaldeído e, principalmente, acetaldeído que apresentou uma maior concentração de formação para os ensaios realizados no Brasil. A formação de aldeídos nos ensaios realizados na Holanda seguiram o mesmo comportamento dos realizados no Brasil, porém, como uma menor formação. Para os ensaios de cloração e ozonização/cloração foi observada a baixa formação de trialometanos. Os testes de toxicidade que usaram como organismo-teste - Daphnia similis - apresentaram toxicidade nos ensaios em que se aplicou 8,0 mg \'O IND.3\'/L, assim como em todas dosagens aplicadas nos ensaios de cloração e, também, para o ensaio de ozonização/cloração para dosagem aplicada de 5,0 mg \'O IND.3\'/L / 10 mg \'CL IND.2\'/L. Em relação ao organismo-teste - Danio rerio - foi detectado toxicidade aguda no ensaio em que se aplicou 5,0 mg \'O IND.3\'/L e tempo de contato 5 minutos e 8,0 mg \'O IND.3\'/L e tempo de contato 15 minutos. / The present work was mostly carried out in Brazil. However, aiming to enhance the research, a six-month data collection was performed at the Wageningen University - the Netherlands. The step carried out in Brazil proposed: to study the formation of by-products (aldehydes and trihalomethanes) from the disinfection of an anaerobic treatment wastewater effluent with ozone, chlorine and ozone/chlorine; to verify how disinfectants act in the oxidation process; to know the degree of toxicity as well as the effects of residual ozone and chlorine employing Daphnia similis and Danio rerio as test-organisms; and, yet, to analyze the efficiency of ozone, chlorine and ozone/chlorine in the inactivation of microorganisms. The step of this research that was carried out in the Netherlands proposed: to study the formation of by-products (aldehydes) from the disinfection of an anoxic treatment effluent with ozone, ozone/chlorine and ozone/hydrogen peroxide (peroxonium); to verify how disinfectants act in the oxidation process; and, to analyze the efficiency of ozone, ozone/chlorine in the inactivation of indicating microorganisms. It was possible to indentify, in the performed studies, an expressive formation of aldehydes with a formaldehyde predominance and, mainly, acetaldehyde that presented a higher formation concentration in the essays carried out in Brazil. The aldehydes formation concentration detected in the essays carried out in The Netherlands followed the same behavior of the ones carried out in Brazil, however with a smaller formation. A low formation of trihalomethanes was observed for the chloration and ozonization/chloration, essays. The toxicity tests that used Daphnia similis as test-organisms presented toxicity in the essays that 8.0 mg \'O IND.3\'/L was applied, as well as for all applied dosages in the chloration essays and, also, for the ozonation/chloration for the applied dosage of 5.0 mg \'O IND.3\'/L / 10 mg \'CL IND.2\'/L. Regarding the Danio rerio test-organism, acute toxicity was detected in the essay in which 5.0 mg \'O IND.3\'/L and contact time of 5 minutes was applied and also for 8.0 mg \'O IND.3\'/L and contact time of 15 minutes.

The need for effective disposal of huge volumes of industrial waste is becoming more challenging due to expected imposition of stringent pollution control regulations in the near future. Thermochemical conversion, particularly gasification of organics in the waste is considered the best route from the perspective of volume reduction and prevalent eco-friendly concept of waste-to-energy transformation. It is considered imperative to have adequate understanding of basic combustion features as a part of the thermochemical conversion process, leading to gasification. The aim of this thesis is to understand the fundamental combustion processes associated with one of the top listed hazardous wastes from distilleries (Biochemical Oxygen Demand (BOD) ~ 40,000 - 50,000 mg/L), commonly known as vinasse, stillage or spent wash, through experiments and modeling efforts. Specially designed experiments on distillery effluent combustion and gasification are conducted in laboratory scale reactors. As an essential starting point of the studies on ignition and combustion of distillery effluent containing solids consisting of 62 ± 2 % organics and 38 ± 2 % inorganics (primarily sugarcane derivatives), the roles of solids concentration, drop size and ambient temperature were investigated through experiments on (1) liquid droplets of 65 % and 77 % solids (remaining water) and (2) spheres of dried effluent (100 % solids) of size 0.5 mm to 20 mm diameter combusted at ambient temperatures of 773 to 1273 K. The investigation reveals that the droplets burn with two distinct regimes of combustion, flaming and char glowing. The ignition delay ‘t1’ of the droplets increased with size as is in the case of non-volatile droplets, while that of bone-dry spheres was found to be independent of size. The ‘t1’ decreased with increase in solids concentration. The ignition delay has showed an Arrhenius dependence on temperature. The initial ignition of the droplets and the dry spheres led to either homogeneous (flaming) or heterogeneous (flameless) combustion, depending on the ambient temperature in the case of sphere and on solid concentration and the ambient temperature, in the case of liquid droplets. The weight loss during the flaming combustion was found to be 50 - 80 % while during the char glowing it was 10-20 % depending on the ambient temperature. The flaming time tc is observed as tc~ d2c , as in the case of liquid fuel droplets and wood spheres. The char glowing time tc' is observed as tc ~ d2c as in the case of wood char, though the inert content of effluent char is as large as 50 % compared to 2 - 3 % in wood char. In the case of initial flameless combustion, the char combustion rate is observed to be lower. The heterogeneous char combustion in quiescent air in controlled temperature conditions has been studied and modeled using one-dimensional, spherico-symmetric conservation equations and the model predicts most of the features of char combustion satisfactorily. The measured surface and core temperatures during char glowing typically are in the range of 200 to 400 K and are higher than the controlled temperature of the furnace. Based on the results of single droplet combustion studies, combustion experiments were conducted in a laboratory scale vertical reactor (throughput ranging from 4 to 10 g/s) with the primary aim of obtaining sustained combustion. Spray of effluents with 50 % and 60 % solids (calorific value 6.8 - 8.2 MJ/kg), achieved by an air blast atomizer, was injected into a hot oxidizing environment to determine the parameters (ambient temperature and air-fuel ratio) at which auto-ignition could occur and subsequently studies were continued to investigate pre-ignition, ignition and combustion processes. Effluent with lower solids concentration was considered first from the point of view of the less expensive evaporator required in the field conditions for concentration and a spin-off in terms of better atomization consequently. Three classes of experiments were conducted: 1) Effluent injection from the wall with no auxiliary heat input, 2) Effluent injection with auxiliary heat input and 3) effluent injection within kerosene enveloping flame. Though individual particles in the spray periphery were found to combust, sustained spray combustion was not achieved in any of the three sets of experiments even with fine atomization. While conducting the third class of experiments in an inclined metallic reactor, sustained combustion of the pool resulting of accumulated spray seemed to result in large conversion of carbon. This led to the adoption of a new concept for effluent combustion in which the residence time is controlled by varying reactor inclination and the regenerative heat transfer from the product gases supplies heat for endothermic pre-ignition process occurring on the bed. Combustion and gasification experiments were conducted in an inclined plate reactor with rectangular cross section (80 mm x 160 mm) and 3000 mm long. A support flame was found necessary in the injection zone in addition to the regenerative heat transfer. Effluent with 60% solids was injected as film on the reactor bed. This film disintegrated into fine particles due to induced aerodynamic stretching and shear stripping. Combustion of individual particles provided exothermic heat profile and resulted into high carbon conversion. However, effluent clogging in the cold injection zone hindered system from attaining steady state. Effluent injected directly on the hot zone caused it to remain mobile due to the spheroidal evaporation and thus assuaging this problem. Improved mass distribution was achieved by displacing nozzle laterally in a cycle, actuated by a mechanism. Consistent injection led to sustained effluent combustion with resulting carbon conversion in excess of 98 %. The typical gas fractions obtained during gasification condition (air ratio = 0.3) were CO2 = 14.0 %, CO = 7.0 %, H2 = 12.9 %, CH4 - 1 % H2S = 0.6 - 0.8 % and about 2 % of saturated moisture. This composition varied due to variation in temperature (± 30 K) and is attributed to combined effect of local flow variations, shifting zones of endothermic processes due to flowing of evaporating effluent over a large area. In order to minimize this problem, experiments were conducted by injecting effluent at higher solids (73 % solids is found injectable). The effluent was found to combust close to the injection location-due to the reduced ignition delay and lower endothermic evaporation load helped raising the local temperature. This caused the pyrolysis to occur in this hottest zone of the reactor with higher heating rates resulting in larger yield of devolatilized products and improved char conversion. Effluent combustion was found to sustain temperature in the reactor under sub-stoichiometric conditions without support of auxiliary heat input and achieved high carbon conversion. These results inspired the use of higher concentration effluent, which is also known in the case of wood to have improved gasification efficiency due to reduction in moisture fraction. In addition, the recent studies on the sulfur emission in the case of black liquor combustion in recovery boilers have revealed that with increase in solids concentration, release of sulfur in gas phase is reduces. The required concentration can be carried out using low-grade waste heat from the reactor itself. It was found through experiments that, even though spray ignition occurred at this concentration, the confined reactor space prevented the spray from attaining sustained combustion. This led to the conduct of experiments in a new vertical reactor with adequate thermal inertia, essential to prevent variations in local temperature to reach a steady state gasification and required space to accommodate the spray. The results of the experiments conducted in the vertical reactor in which effluents with 73 % solids, heated close to the boiling point and injected as fine spray in a top-down firing mode are consolidated and reported in the thesis in detail. Single particle combustion with enveloping faint flame was seen unlike stable flame found in coal water slurry spray combustion. Sustained gasification of gas-entrained particles occurred at reactor temperature in the range of 950 K - 1000 K and sub-stoichiometric air ratio 03 - 0.35 without the support of auxiliary fuel. The typical gas fractions obtained during gasification condition (air ratio = 0.3) were CO2 = 10.0 -11.5 %, CO - 10.0 - 12.0 %, H2 - 6.7 - 8.0 %, CH4 = 1.75 % H2S = 0.2 - 0.4 % and about 2 % of saturated moisture. The carbon conversion obtained was in the range of 95 - 96 %. These experiments have provided the conditions for gasification. The extraction of potassium salts (mostly sulfates, carbonate and chloride) from the ash, using a simple water leaching process, was found to recover these chemicals to as high an extent as 70 - 75 % of total ash. In summary it is concluded that increasing the solid concentrations to as high levels as acceptable to the system (~ 75 %) and introducing as a fine spray of heated material (~ 363 K) into furnace with air at sub-stoichiometric conditions in a counter current combustion reactor will provide the frame work for the design of a gasification system for vinasse and similar effluent material. The thesis consists of seven chapters. Chapter 1 introduces the problem and motivation of the work presented in the thesis. Literature review is presented in Chapter 2. The Chapter 3 deals with the single particle combustion studies. The results of effluent spray combustion experiments conducted in a laboratory scale vertical reactor are presented in Chapter 4. The results of combustion and gasification experiments conducted in another variant of a reactor, namely, inclined flat plate rectangular reactor is consolidated in Chapter 5. The results of gas-entrained spray gasification experiment of higher concentration effluent injected as spray in the vertical reactor are presented in Chapter 6. The general conclusions and scope for the future work are presented in the concluding chapter 7.

Time-consuming and expensive benthic surveys are currently the most common means of determining impacts on invertebrates and fish habitat in lotic systems. We propose using the rate of chitobiase production by benthic invertebrates as a complement for determining impacts on freshwater systems. We successfully modified the existing assay to a microplate approach for high throughput analysis of chitobiase activity. Next we conducted two case studies in: 1) the Dead Horse Creek, Manitoba, to determine if changes in chitobiase could detect impacts on the benthic community from wastewater effluent and; 2) in Snake and Kinch Creeks, Manitoba to see if chitobiase could be used to assess fish habitat quality. In both cases, we observed no strong relationships between chitobiase and traditional metrics (e.g., abundance, biomass, diversity). We recommend further studies concerning the timing of chitobiase release in lotic systems and assessments of its use in mesocosm and microcosm toxicity studies / May 2016

La recherche sur le traitement des eaux usées industrielles prend de plus en plus d’importance à cause de la complexité des effluents que les industries rejettent. Parmi ces effluents, 5% (v/v) ont une salinité variant entre 3 et 350 g/L en chlorure de sodium (NaCl), la salinité étant la quantité de sels minéraux dissous dans l'eau. Les réglementations environnementales sont de plus en plus strictes de sorte que les procédés de traitement utilisés pourraient devenir inappropriés. Les effluents salins en particulier sont souvent incapables de satisfaire les réglementations de rejet des eaux usées, à cause de leur difficulté de traitement dûe au mélange complexe de matière organique et de sel. Le bon fonctionnement des procédés biologiques conventionnels est souvent négativement affecté par la présence de ce dernier. C’est donc vers les procédés physico-chimiques que les industries se sont tournées pour traiter les effluents salins. Mais ceux-ci étant très coûteux en termes d’opération et de maintenance, la recherche s’est concentrée sur la faisabilité du traitement d’effluents salins par procédés biologiques, plus économiques. Les nouvelles recherches sur des bactéries résistantes au sel (halophiles et halotolérantes) appliquées aux traitements biologiques, bien que peu nombreuses encore, sur la sélection bactérienne et la bioaugmentation ouvrent de nouvelles possibilités quant au traitement biologique de la matière organique présente dans les effluents salins. Cette étude a donc pour objectif principal de valider la biofiltration aérobie pour le traitement du méthanol à l’état liquide en milieu salin. Pour cela, on a réalisé le suivi de divers paramètres opératoires (concentration du méthanol à l’entrée du réacteur, charge organique, teneurs en sel). Le développement de cette technologie serait une innovation dans le traitement des effluents industriels, puisque l’application de la biofiltration au traitement de ce type d’effluent n’a jamais été étudiée. La biofiltration présente des avantages économiques comparativement aux technologies utilisées jusqu’à présent. Cette étude a permis d’obtenir une efficacité d’élimination du méthanol satisfaisante (de l’ordre de 54%) pour un effluent contenant des concentrations élevées en sel (30 g/L) sous forme de NaCl, et en méthanol 5 (g/L) pour un débit d’alimentation liquide de 5 L/j.