A presença de resíduos de fármacos em águas superficiais e de abastecimento público tem preocupado a comunidade científica devido principalmente à sua persistência na água e aos efeitos adversos causados à comunidade aquática e aos possíveis riscos à saúde humana. Dentre os fármacos comumente identificados em águas de abastecimento público, encontram-se os anti-inflamatórios, como o diclofenaco (DCF), um dos fármacos mais consumidos no Brasil e no mundo. Nesse contexto, o presente trabalho, teve como objetivo principal estudar a eficiência das etapas de tratamento de água em ciclo completo (coagulação, floculação, sedimentação, filtração em areia e desinfecção com cloro) com e sem pré-oxidação com cloro e com dióxido de cloro e adsorção em carvão ativado granular (CAG) na remoção de DCF. Também foram determinados os trialometanos (THM) e identificados os principais subprodutos do DCF formados na oxidação com cloro e dióxido de cloro. Para a determinação do DCF nas amostras de água antes e após as etapas de tratamento de água foram desenvolvidos e validados métodos analíticos de extração em fase sólida (SPE) e cromatográfico por cromatografia líquida de alta eficiência (HPLC) com detecção no ultravioleta (UV). A validação do método foi feita de acordo com a resolução n&ordm; 899 de 2003 da Agência Nacional de Vigilância Sanitária (ANVISA), considerando os requisitos para métodos bioanalíticos. Os procedimentos analíticos empregados foram efetivos e confiáveis para a identificação e quantificação do DCF nas amostras de água antes e após os processos de tratamento de água. Os ensaios de tratamento de água foram feitos em equipamento de reatores estáticos (jarteste) e filtros de escala laboratorial empregando-se água de poço artesiano não clorada preparada com substâncias húmicas aquáticas (SHA) para conferir cor verdadeira de 20 uH, caulinita para conferir turbidez de 70 uT e fortificada com 1 mg L-1 de DCF. Os resultados indicaram que as etapas de coagulação com sulfato de alumínio, floculação, sedimentação e filtração em areia não removeram o DCF. Nas etapas de préoxidação com cloro e dióxido de cloro e de pós-cloração houve remoção parcial do DCF, porém verificou-se a formação de subprodutos provenientes da oxidação do DCF. Dentre os THM, foi quantificado apenas o clorofórmio na etapa de pré-oxidação com cloro. Em geral, os resultados indicaram que o dióxido de cloro foi mais eficiente na redução do DCF e formou menos subprodutos. Entretanto, o tratamento em ciclo completo seguido da adsorção em CAG foi eficiente na remoção de DCF, com remoção maior que 99,7%. Os subprodutos formados na oxidação com cloro e dióxido identificados por cromatografia líquida acoplada a espectrometria de massas em série (LC-MS/MS) consistiram na descaboxilação/hidroxilação e substituição aromática de átomos de hidrogênio por cloro. Os subprodutos identificados na oxidação com cloro apresentaram as seguintes fórmulas moleculares: C14H11</subCl2NO3, C13H10Cl3N e C14H10Cl3NO2. Com o dióxido de cloro foi identificado o subproduto de fórmula molecular igual a C14H11Cl2NO3. / The presence of pharmaceutical residues in surface waters and in drinking water supply has concerned the scientific community, mainly in which regards their persistence in water, adverse effects on the aquatic community and possible risks to human health. Antiinflammatory drugs, as diclofenac (DCF), are among those drugs commonly identified in drinking water supply. In this context, the main objective of this study was to assess the efficiency of the different stages of the conventional drinking water treatment (coagulation, flocculation, sedimentation, sand filtration and chlorine disinfection) with and without preoxidation with chlorine and chlorine dioxide and adsorption on granular activated carbon (GAC) in the removal of DCF. The trihalomethanes (THMs) were also determined and the main by-products of DCF formed by oxidation with chlorine dioxide and chlorine were identified. For the DCF determination in water samples before and after water treatment stages analytical methods of solid phase extraction (SPE) and chromatographic method by high performance liquid chromatography (HPLC) with detection in the ultraviolet (UV) were developed and validated. The method validation was based on Resolution n&ordm; 899 of the 2003 of the Brazilian National Health Surveillance Agency (ANVISA), considering the requirements for bioanalytical methods. The analytical procedures used were effective and reliable for the identification and quantification of DCF in the water samples before and after the water treatment stages. The water treatment tests were carried out in jar test equipment and filters on laboratory scale employing non chlorinated water of artesian well prepared with aquatic humic substances (AHS) to yield 20 uH true color, kaolin turbidity of 70 NTU and DCF concentration of 1 mg L-1. The results indicated that the stages of coagulation with aluminum sulphate, flocculation, sedimentation and filtration sand did not remove DCF. In the stages of pre-oxidation with chlorine and chlorine dioxide and chlorine disinfection the DCF was partially removed, however by-products were formed from the DCF oxidation. Among the THMs, only chloroform was quantified in the pre-oxidation with chlorine. In general, the results showed that chlorine dioxide was more effective to reduce the DCF and fewer by-products were formed. Nevertheless, the complete cycle treatment followed by GAC adsorption was effective to remove DCF (&gt; 99.7%. removal). The by-products of the oxidation of DCF with chlorine and chlorine dioxide identified by liquid chromatography coupled tandem mass spectrometry (LC-MS/MS) consisted in the descaboxylation/hydroxylation and aromatic substitution of hydrogen atoms by chlorine. The compounds identified in the oxidation with chlorine showed the following molecular formulas: C14H11</subCl2NO3, C13H10Cl3N e C14H10Cl3NO2. The by-product identified using chlorine dioxide was C14H11Cl2NO3.

Bei der Aufbereitung von Rohwässern zu Trinkwasser fallen in der Regel unvermeidbare Rückstände an, die den gesetzlichen Bestimmungen entsprechend entsorgt werden müssen. Schlammhaltige Wässer, die den größten Anteil an Wasserwerksrückständen einnehmen, entstehen bei der Spülung von Filtern und enthalten nahezu alle aus dem Rohwasser entfernten Stoffe und nicht im Trinkwasser verbleibende Aufbereitungschemikalien. Während früher in vielen Wasserwerken Teile des schlammhaltigen Filterspülwassers nach einem Sedimentationsvorgang wieder in den Aufbereitungsprozess zurückgeführt wurden, ist dies in Deutschland auf Grund einer möglichen Beeinträchtigung der Trinkwasserqualität bei mikrobiologisch belasteten Wässern (z. B. Oberflächenwasser) ohne eine adäquate Behandlung (z. B. Ultrafiltration) nicht mehr erlaubt. Somit müssen schlammhaltige Filterspülwässer anderweitig entsorgt werden, z. B. durch eine Einleitung in die Kanalisation. Die dabei auftretenden Auswirkungen auf Abwasserbehandlungsanlagen sind noch nicht ausreichend bekannt. In der vorliegenden Arbeit werden unterschiedliche Ultrafiltrationsmodule (Kapillarmembranmodul und getauchtes Modul) hinsichtlich ihrer Eignung zur Aufbereitung aluminiumhaltiger schlammhaltiger Filterspülwässer und damit zur Rückführung des entstehenden Filtrates in den Aufbereitungsprozess untersucht. Die grundsätzliche Eignung beider Modulsysteme wird nachgewiesen. Bei Verwendung von getauchten Modulen kann auf eine vorangehende Sedimentationsanlage verzichtet werden. Als kritisch muss unabhängig vom gewählten Modulkonzept die Entsorgung des anfallenden Retentates angesehen werden, da die gesetzlich vorgeschriebenen Grenzwerte der Indirekteinleitung für mehrere Parameter nicht eingehalten werden. Bilanzierungen der relevanten Schadstoffe ergeben, dass der Schadstoffeintrag überwiegend diffus mit dem Rohwasser in das Wasserwerk erfolgt. Zur Untersuchung von Auswirkungen der Einleitung aluminiumhaltiger schlammhaltiger Filterspülwässer aus der Oberflächenwasseraufbereitung auf die Abwasserbehandlung wurden labortechnische Versuche zur Ermittlung des Phosphatadsorptionspotenzials durchgeführt. Neben der Abhängigkeit der Phosphatadsorptionskapazität vom pH-Wert wurde der Einfluss der Feststoffkonzentration des schlammhaltigen Filterspülwassers in Versuchen mit Modellwasser nachgewiesen. Eine Erhöhung der Feststoffkonzentration wirkt einer möglichst hohen Ausnutzung des Adsorptionspotenzials entgegen. Während für die Ultrafiltrationsbehandlung gegenüber der Indirekteinleitung ein Kostenvorteil ermittelt wird, ist die für die Nutzung des Phosphatadsorptionsanteils verfügbare Schlammmenge für einen alleinigen Einsatz in der Kläranlage bei gleichen Einzugsgebieten nicht ausreichend. / In most water treatment plants (WTPs), during the water purification process, residuals are generated that have to be disposed according to current regulations. Most of the residuals are derived from filter backwash processes (i. e. spent filter backwash water, SFBW) and contain substances that are removed from the raw water. In addition, in the spent filter backwash water, chemicals can be found that are required for the operation of the water treatment process and do not remain in the drinking water. Over recent decades, SFBW has been returned to the beginning of the water treatment plant (WTP) after a sedimentation process in order to reduce the amount of water being discharged. Concerns over the recycling of microorganisms, of heavy metals or precursors for disinfection by-products, have led to a significant reduction of the number of WTPs that directly return filter backwash water to the water treatment process. According to German technical standards, the reuse of SFBW might only be possible after the application of groundwater infiltration or an equivalent technique. Because of an almost complete recovery of particles and microorganisms, ultrafiltration treatment is a proven alternative to groundwater recharge of SFBW. In this work, different ultrafiltration modules for the treatment and reuse of SFBW are compared. Capillary as well as submerged membrane modules are suitable for the treatment of SFBW. If submerged membrane modules are used, no sedimentation period prior to ultrafiltration treatment is necessary. As a consequence of the accumulation of particulate matter including heavy metals and other compounds in the retentate during ultrafiltration treatment, threshold values of several regulations cannot be met, and either the discharge of retentate into the sewer will be charged or alternative disposal options must be considered. Mass balances for an entire WTP showed most of these contaminants to originate from non-point sources in the watershed. Lab-scale experiments are performed for the examination of the phosphate adsorption potential of SFBW derived from surface water treatment using aluminum-based coagulants. Besides a strong influence of the pH-value present in the SFBW, an influence of the TSS-concentration of SFBW on phosphate adsorption capacity could be demonstrated. Elevated TSS-concentrations resulted in a lower phosphate adsorption capacity of the investigated SFBW. While ultrafiltration treatment with subsequent reuse of SFBW might be cheaper than the discharge to the sewer system, the amount of SFBW required for a complete phosphate removal in the wastewater treatment plant is to large and therefore, no economic advantage of phosphate adsorption could be demonstrated

<p>Volcanic ash and Moringa oleifera (M. oleifera) were investigated as indigenous materials for drinking water treatment based on problems identified at Kampala and Masaka water treatment plants in Uganda. Coagulation experiments were done using swamp raw water at Masaka National Water & Sewerage Corporation water treatment plant and pilot-scale filtration experiments carried out at Ggaba II (Kampala) water treatment plant. The results from the study indicated that there were both operational and design handicaps at the treatment plants in Kampala. There is need to modify the filtration and clarification units to enable production of water meeting both the national and international standards. At Masaka water treatment, there was increase in trihalomethanes concentration as a result of pre-chlorination. Following aeration and pre-chlorination processes, the average increase of total trihalomethanes concentration was over 4000% with over 99% being chloroform. Preliminary results from the jar test experiments indicated that use of alum with MOCSC as coagulant aid is promising as a first stage in the treatment train for waters with a humic materials and high content of iron, typical of swamp water sources. This would probably eliminate the formation of unwanted by-products by eliminating the pre-chlorination process. Assessment of the characteristics of the volcanic ash showed that it meets the requirements for a filtration material; and results obtained from the pilot study showed that it was a suitable alternative material for use in a dual media filtration system. There was an increase in the filter run length of about two and half fold in the dual media filtration column compared to the mono medium column. Both columns produced similar water quality levels. Therefore, conversion of the rapid sand filters at Ggaba and similar water treatment plants in the country to dual media (volcanic ash on top of sand) systems would probably significantly improve the performance of the filtration systems.</p>

The objective of this research was to develop fluorescence-based tools that are suitable for performing rapid, accurate and direct characterization of natural organic matter (NOM) and colloidal/particulate substances present in natural water. Most available characterization methods are neither suitable for characterizing all the major NOM fractions such as protein-, humic acid-, fulvic acid- and polysaccharide-like substances as well as colloidal/particulate matter present in natural water nor are they suitable for rapid analyses. The individual and combined contributions of these NOM fractions and colloidal/particulate matter present in natural water contribute to membrane fouling, disinfection by-products formation and undesirable biological growth in drinking water treatment processes and distribution systems. The novel techniques developed in this research therefore, provide an avenue for improved understanding of these negative effects and proactive implementation of control and/or optimization strategies. The fluorescence excitation-emission matrix (EEM) method was used for characterization of NOM and colloidal/particulate matter present in water. Unlike most NOM and colloidal/particulate matter characterization techniques, this method can provide fast and consistent analyses with high instrumental sensitivity. The feasibility of using this method for monitoring NOM at very low concentration levels was also demonstrated with an emphasis on optimizing the instrument parameters necessary to obtain reproducible fluorescence signals. Partial least squares regression (PLS) was used to develop calibration models by correlating the fluorescence EEM intensities of water samples that contained surrogate NOM fractions with their corresponding dissolved organic carbon (DOC) concentrations. These fluorescence-based calibration models were found to be suitable for identifying/monitoring the extent of the relative changes that occur in different NOM fractions and the interactions between polysaccharide- and protein-like NOM in water treatment processes and distribution systems. Principal component analysis (PCA) of fluorescence EEMs was identified as a viable tool for monitoring the performance of biological filtration as a pre-treatment step, as well as ultrafiltration (UF) and nanofiltration (NF) membrane systems. The principal components (PCs) extracted in this approach were related to the major membrane foulant groups such as humic substances (HS), protein-like and colloidal/particulate matter in natural water. The PC score plots generated using the fluorescence EEMs obtained after just one hour of UF or NF operation could be related to high fouling events likely caused by elevated levels of colloidal/particulate-like material in the biofilter effluents. This fluorescence EEM-based PCA approach was sensitive enough to be used at low organic carbon levels present in NF permeate and has potential as an early detection method to identify high fouling events, allowing appropriate operational countermeasures to be taken. This fluorescence EEM-based PCA approach was also used to extract information relevant to reversible and irreversible membrane fouling behaviour in a bench-scale flat sheet cross flow UF process consisting of cycles of permeation and back-washing. PC score-based analysis revealed that colloidal/particulate matter mostly contributed to reversible fouling, while HS and protein-like matter were largely responsible for irreversible fouling. This method therefore has potential for monitoring modes of membrane fouling in drinking water treatment applications. The above approach was further improved by utilizing the evolution of the PC scores over the filtration time and relating these to membrane fouling by the use of PC scores??? balanced-based differential equations. Using these equations the proposed fluorescence-based modeling approach was capable of forecasting UF fouling behaviours with good accuracy based solely on fluorescence data obtained at time = 15 min from the initiation of the filtration process. In addition, this approach was tested experimentally as a basis for optimization by modifying the UF back-washing times with the objective of minimizing energy consumption and maximizing water production. Preliminary optimization results demonstrated the potential of this approach to reduce power consumption by significant percentages. This approach was also useful for identifying the fouling components of the NOM that were contributing to reversible and irreversible membrane fouling. Grand River water (Southwestern Ontario, Canada) was used as the natural water source for developing the techniques presented in this thesis. Future research focusing on testing these methods for monitoring of membrane fouling and treatment processes in large-scale drinking water treatment facilities that experience different sources of raw water would be useful for identifying the limitation of these techniques and areas for improvements.

Submitted in fulfillment of the academic requirement for the degree Master of Engineering in Chemical Engineering, Department of Chemical Engineering, Faculty of Engineering and the Built Environment, Durban University of Technology, Durban, South Africa, 2017. / Provision of microbiologically safe drinking water for people living in the rural areas of developing countries remains a major challenge to date. One of the reasons is due to the inability to access potable water mainly because of poor existing water purification systems. Current measures have been put in place to address the challenges of rural water supply. Development of appropriate technologies such as decentralized water treatment supply in the form of point of use (POU) systems are been considered. In lieu of the above, an appropriate POU system known as the Remote Rural Water Treatment System (RRWTS) was developed at Durban University of Technology (DUT). The RRWTS is polyester based locally sourced Woven Fabric Microfiltration (WFMF) membrane system. The unit is made up of flat sheet modules that are assembled into a pack. It is a robust gravity driven system with the ability to remove suspended solids and colloids in the form of turbidity. The system has high flux of 35 ± 7 LMH and turbidity below 1 NTU, it has the ability to remove pathogens well above 95%. However, this does not comply with WHO and SANS drinking water standards of zero E. coli count/100 ml of treated water. In order to bring the water treated by RRWTS to a satisfactory level for drinking, it is then necessary to add a separate disinfection step like chlorination step to further remove the remaining microbial contaminants. Thus the main objective of the study was to evaluate the disinfection efficacy of two disinfectants namely waterguard and bromochlor tablet disinfectants and investigate their integration with the WFMF membrane. The study was categorised into three parts. The first part is the addition of disinfectants to unfiltered river water sources for the determination of residual chlorine and the most optimum dose that will yield effective disinfection and also evaluate the extent of E. coli removal by the disinfectants. The second stage was the filtration of four river water sources using the woven fibre membrane (WFM) to determine the efficiency of WFMF. Finally the effect of disinfection kinetics on disinfection was achieved by agitating the water after disinfection and allowing it to stand at different contact times. Performance of the RRWTS was determined by the amount of E. coli and turbidity removed during filtration using WFMF and by chemical disinfectants after filtration. The results on residual chlorine for different water sources showed that feed quality and disinfectant dose determines the quantity of residual chlorine on all the water sources. The effectiveness of chemical disinfectants in E. coli removal is affected by the quality of water to be disinfected. The study showed that turbidity plays a major role on disinfection by increasing chlorine demand on water sources with high turbidity levels. The WFMF demonstrated excellent filtration performance by producing permeates with turbidity less than 1 NTU for feed turbidities ranging from 10 to 200 NTU. The E. coli removal efficiency by WFMF was very high on all the water sources treated. There was 95-99.8% E. coli removal on raw feeds with influent E. coli ranging between 500 and 44500 CFU/100 ml. It was seen that major benefits are derived from integrating the WFMF (RRWTS) with chemical disinfection. The benefits includes; better disinfection that meets drinking water set guidelines of zero E. coli and improved quality of water. The need for disinfection kinetics in order to obtain superior disinfection was eliminated. The possibility of disinfection-by-product formation was reduced as smaller quantities of chemical disinfectants were required for complete disinfection on the filtered water. / M

M.Sc. / The world is focusing on increasing the number of people who have access to safe drinking water due to the ascending numbers of drinking water related illnesses reported annually in rural areas where water is not treated before consumption. To meet this goal, household water treatment has to be introduced especially in places where homes are wide apart making centralised water treatment improbable. Most readily available household water treatment systems (HWTS) such as membrane filters may not be affordable in rural areas due to power requirements and degree of ability to use and maintain them. This study was therefore aimed at designing and constructing HWTS using readily available material such as sand, gravel, zeolites and clays. Five HWTS were designed, built, evaluated and compared based on their ability to remove chemical contaminants such as iron, arsenic and fluorides from drinking water. The types of filters that were used during this study are the biosand filter (BSF), a modified biosand filter with zeolites (BSFZ), a silver impregnated porous pot (SIPP) filter, a ceramic candle filter (CCF) and a bucket filter (BF). Effectiveness of the filters in reducing physical parameters such as turbidity and visual colour was also assessed. The water treatment devices had the following flow rates; 1.74 L/h – 19.20 L/h (BSFZ), 0.81 L/h – 6.84 L/h (BSF), 0.05 L/h – 2.49 L/h (SIPP) and 1.00 L/h – 4.00 L/h (CCF). The flow rates were high at the early stages of filter use and decreased with increase in the volume of water filtered through. The flow rates of the filters were affected by the turbidity of intake water which was between 1.74 NTU – 42.93 NTU and correlated to chlorophyll a concentrations. The household water treatment technologies reduced turbidity to levels less than 1 NTU (> 90% reduction) in the following order SIPP > BSFZ > BSF > CCF > BF. The filters achieved greater than 60% retention of calcium, magnesium, iron and arsenic. These contaminants with the exception of arsenic were reduced to acceptable levels of the South African National Standard of drinking water (SANS 241, 2004). Compared to the other filters, the BSFZ performed better in removing nitrates, phosphates and fluorides although the overall retention efficiency was low. Total organic carbon was removed greatly by the CCF (39%) and the least removal was by the BF. The overall performance of the filters in reducing contaminants from drinking water was in the order BSFZ > BSF > SIPP > CCF > BF. Filter washing vi resulted in an overall increase in the flow rates of the filters but negatively affected turbidity reduction. The filters still removed contaminants after total cumulative volumes of 1200 L (BSFZ, BSF, CCF and BF) and 300 L (SIPP) were filtered through the devices. The five evaluated filters have several advantages to the readily available technologies and the advantages include ease of construction, operation and maintenance. The filters are gravity driven and work independent of temperature. These HWTS incorporate safe storages fitted with spigots to eliminate recontamination of water when it is drawn for use. The filters can produce enough drinking and cooking water for a family of six members due to their high flow rates. The BSFZ, BSF, SIPP, CCF and BF may therefore be considered for treating contaminated water at household scale in places where water is taken directly from the source without treatment.

Orientador: Wilson de Figueiredo Jardim / Tese (doutorado) - Universidade Estadual de Campinas, Instituto de Química / Made available in DSpace on 2018-08-26T13:39:08Z (GMT). No. of bitstreams: 1 Pescara_IgorCardoso_D.pdf: 5286232 bytes, checksum: 74793adc4ea590e2eb8fdeb51a796399 (MD5) Previous issue date: 2014 / Resumo: Este trabalho teve como objetivo avaliar a eficiência dos tratamentos empregados em cinco estações de tratamento de esgoto (ETE) e duas estações de tratamento de água (ETA) na remoção dos hormônios endógenos estrona (E1), 17?-estradiol (E2), estriol (E3), testosterona (TTN) e progesterona (PROG), hormônios sintéticos 17a-etinilestradiol (EE2), dietilestilbestrol (DES), norgestrel (NGT) e mestranol (MEE), produtos de uso industrial bisfenol A (BPA), fenolftaleína (PhPh), n-nonilfenol (nNP), n-octilfenol (nOP) e triclosan (TCS), o fármaco cafeína (CAF) e o pesticida atrazina (ATZ). Foi possível quantificar BPA, E1, E3, CAF e ATZ em esgoto bruto e BPA, E1, CAF e ATZ em água bruta. Para cada composto, tanto os tratamentos realizados pelas ETE quanto os realizados pelas ETA apresentaram eficiências de remoção variáveis. A cafeína foi o composto-alvo mais frequentemente encontrado nas amostras, sendo escolhida como indicador químico para avaliar a eficiência dos tratamentos. Foi encontrada uma taxa média de 99% para a remoção de CAF pelas ETE, sendo as etapas com tratamentos biológicos as mais eficientes. Os tratamentos anaeróbios apresentaram remoções médias superiores a 80% na remoção de CAF, e os tratamentos aeróbios foram capazes de remover cerca de 20% da carga do composto. Nas ETE, os tratamentos de coagulação e desinfecção foram pouco eficientes nas remoções dos compostos-alvo. Já para as ETA, foram observadas remoções de até 80% de CAF pelos tratamentos empregados, sendo a etapa de coagulação a responsável pela maior remoção de CAF da água bruta. A etapa de filtração em carvão ativado apresentou eficiências de remoção menores que 10%, enquanto a desinfecção demonstrou baixa eficiência na remoção de CAF. Na cidade de São José do Rio Preto ¿ SP foi possível quantificar, ao menos uma vez, BPA, E1, E3, PhPh, CAF, TCS e ATZ em água superficial, BPA, TCS e CAF em água subterrânea e BPA, CAF e ATZ em água de abastecimento. / Abstract: Water and wastewater conventional treatments are often considered inefficient to remove micropollutants. The aim of this work was to evaluate the removal efficiency of the endogenous hormones estrone (E1), 17? estradiol (E2), estriol (E3), testosterone (TTN), and progesterone (PROG), the synthetic hormones 17a-ethinylestradiol (EE2), diethylstilbestrol (DES), norgestrel (NGT), and mestranol (MEE), the industrial chemicals bisphenol A (BPA), phenolphthalein (PhPh), n nonylphenol (nNP), n octylphenol (nOP), and triclosan (TCS), the pharmaceutical caffeine (CAF), and the pesticide atrazine (ATZ) by five wastewater treatment plants (WWTP) and two drinking water treatment plants (DWTP). The target compounds BPA, E1, E3, CAF, and ATZ were found in raw sewage, while BPA, E1, CAF, and ATZ in raw water. Both WWTP and DWTP treatments presented variable removal efficiency. Caffeine was the target compound more often detected in samples, thus it was chosen as a chemical indicator to evaluate treatment efficiencies. The average removal of CAF by WWTP was 99%, in which the biological treatment was more efficient. The anaerobic treatment presented an average removal of CAF above 80%, and around 20% for the aerobic treatments. Coagulation and disinfection treatments of WWTP showed low efficiency to remove the target compounds. DWTP treatment efficiency reached up to 80% removal, with coagulation step presenting highest removals of CAF. The activated carbon filtration showed removal efficiency under 10%, whereas the disinfection step presented low efficiency to remove CAF. At São José do Rio Preto city were found, at least once, BPA, E1, E3, PhPh, CAF, TCS, and ATZ in surface water; BPA, TCS, and CAF in groundwater, and BPA, CAF, and ATZ in drinking water / Doutorado / Quimica Analitica / Doutor em Ciências

This diploma thesis deals with the efficiency of removal of pharmaceuticals from drinking water by selected adsorption materials. The first part describes sources of pharmaceuticals in drinking water and possible ways of contaminating water by pharmaceuticals. Subsequently, the pharmaceuticals most commonly found in the environment - nonsteroidal anti-inflammatory drugs, antibiotics, psychiatric drugs and sex hormones - are described in more detail. Next, the thesis describes the processes used for removal of pharmaceuticals. These are activated carbon adsorption, membrane processes and advanced oxidation processes. The last chapter of the theoretical part of the thesis deals with water treatment plants, where the technologies for removing drugs are already in operation. In the practical part of this thesis an experiment was performed and evaluated, for a purpose of comparing the efficiency of selected sorption materials in the removal of diclofenac from water. Filtrasorb F100, Bayoxide E33 and GEH were used.

The main theme of this thesis is the usage of the test investigating the formation potential of trihalogenmethanes (THM FP) and its comparison with conventional indicators of water quality (CODMn, A254 and colours). As for the experimental part of the thesis, rating of the effectiveness of selected technological procedures has been applied (e.g.: coagulation, adsorption and ozonation in the act of treatment of artificially prepared water model with a higher content of humic substances in laboratory conditions). Based on the obtained results, it was found that the common indicators of water quality have very similar attributes and also complete each other. On the contrary, those attributes of indicators may not be sufficient in case of the evaluation of water quality with high content of humic substances. The findings made illustrate that the THM FP test enables the accurate evaluation of water quality, especially in connection with the content of an organic material susceptible to chemical changes. THM formation potential has proved its high value and also has confirmed that it can appropriately complete the other standarts that are being used for assessing the quality of treated water up to nowadays.

This thesis is focused on technological processes during drinking water treatment. The emphasis is put on monitoring indicators of organic substances present in water and indicators of the biological stability of treated water. The experimental part is focused on the comparison of separation efficiency of drinking water treatment technological processes by monitoring of chemical oxygen demand, absorbance measured at 254 nm, bioseston, culturable microorganisms and assimilable organic carbon.