Made available in DSpace on 2014-10-09T12:38:36Z (GMT). No. of bitstreams: 0 / Made available in DSpace on 2014-10-09T14:04:36Z (GMT). No. of bitstreams: 1 06057.pdf: 4829282 bytes, checksum: d92eb047d0390013a61d21a5e1144641 (MD5) / Dissertacao (Mestrado) / IPEN/D / Instituto de Pesquisas Energeticas e Nucleares - IPEN/CNEN-SP

M.Ing. / The Rietvlei Water Treatment Plant was extended with a granular activated carbon (GAC) filtration system after an exhaustive series of tests, which were started in 1994. Upon commissioning towards the middle of 1999, a year of close monitoring followed to measure the GAC performance at full-scale. After verification that the GAC does indeed ensure a high quality product under all conditions, the emphasis shifted to the optimisation of the GAC handling and regeneration system. Frequently moving the entire GAC inventory from the filters to an off-site regeneration plant and back requires significant operational effort and contributes a major part of the total cost of the GAC system. A number of systematic investigations were carried out in response to a number of practical questions that arose at Rietvlei. The first part of the study was directed towards tracking and quantifying the GAC on and off site. The main findings were that 10.0% of the GAC is lost from the filter during backwashing (0.3%) and removal of GAC from the filter for regeneration (9.7%). The sump traps not all this GAC and 2.3% of the total inventory is lost to the river. Inserting a sieve at the outlet of the sump can eliminate this loss. A further 80.3% of the GAC in a filter is removed for regeneration, of which 18.7% is lost during the regeneration process. The minimising off this loss can only be achieved through the optimisation of the regeneration process, which falls within the domain of the regeneration contractor. The second part of the study was directed at the behaviour of the GAC whilst within the filter bed. The porosity and sphericity was determined by laboratory tests and calculations. The porosity was found to be 0.69 for the 12 x 40 size carbon and 0.66 for the 8 x 30 size carbon and the sphericity was found to be 0.67 for the 12 x 40 size carbon and 0.66 for the 8 x 30 size carbon. By using a calibrated bed expansion model, the bed expansion could be calculated at 9°C and 23°C for the two carbons gradings; the maximum temperature range experienced at Rietvlei. The main finding of this part of the study was that the average available freeboard is 650 mm for the 12 x 40 grading and 430 mm for the 8 x 30 grading, and therefore no GAC should wash over the weir at all during backwashing. The third part of the study measured the physical changes of the GAC found at different points in the GAC cycle. The main findings were that the small fraction of GAC washed out of the bed during backwashing and removal has a finer grading, higher apparent density and lower adsorption capacity than the GAC in the filter bed. There seems to be no marked attrition of the carbon or generation of fines during the removal and transport of the GAC to the regeneration plant. After regeneration, there was a 7% decrease in apparent density and a 30% increase in adsorption capacity. The final part of the study correlated the adsorption capacity of the GAC with its time in use as well as UV254 removal. After regeneration, UV254 removal begins at approximately 20% and declines to 14% after 400 days of operation, and to 10% after 600 days. After regeneration, the iodine number begins at approximately 800, declines to 600 after 400 days of operation, and to 500 after 600 days.

Nitrogen is an essential nutrient for plant and animal life; however, its presence in concentrations exceeding assimilative capacities of receiving water bodies is undesirable. Therefore, the form and concentration of total nitrogen released in wastewater effluents is of great concern. During the course of this study, the nitrogen analysis was performed on the various unit processes of the Florida Technological University wastewater treatment plant. The average percent removal of nitrogen between plant influent and clarifier effluent was 30.5% during the month of August 1975. It is believed that the nitrogen removal is attributed to luxury uptake by the biomass through the plant. The clarifier effluent was highly nitrified containing an average ammonia nitrogen concentration of 0.76 milligrams per liter and a nitrate nitrogen concentration of 16.47 milligrams per liter. The extent to which nitrification took place was 93 - 98% with an average of 96.5% for the month of August.

The dewatering characteristics of polyaluminum chloride (Hyper⁺Ion 1050A) sludges were investigated using lab-scale tests including specific resistance to filtration (r*), capillary suction time (CST), and sludge pH. The effects of chemical conditioning (lime and cationic polymer) and mixing intensity (Gt) upon the sludge dewatering characteristics in a pilot-scale plate and frame press were also studied. The dewatering characteristics of the Hyper⁺Ion sludges were found to be dependent upon the influent water turbidity conditions; specifically, the ratio of aluminum coagulant to total dry solids in the sludge. Lime was an effective conditioner for doses that produced a sludge pH value in the range of 11.5 to 11.8 which, again, was a direct function of the aluminum coagulant fraction in the sludge. Cationic polymer and a combination of lime and polymer were also effective conditioning schemes when the appropriate dose and mixing intensity were applied. / Master of Science

The effects of four oxidants upon water treatment process parameters were investigated. The four oxidants under consideration were ozone, chlorine dioxide, potassium permanganate, and chlorine, Experimentation was directed towards the impact of these oxidants upon turbidity, TOC, and color removal, as well as reduced manganese oxidation. Studies were conducted with an experimental water with enhanced TOC levels. Experimentation was accomplished by a series of jar tests in which solution pH, coagulant dose, and oxidant dose were varied. Results show that, in general, oxidant application had either no impact or a negative impact upon TOC, turbidity, and color removal. Further deterioration of finished water quality was observed with increasing oxidant dose. Reduced manganese was oxidized by both potassium permanganate and chlorine dioxide. Ozone effectively oxidized reduced manganese in waters of low TOC, while chlorine was an ineffectual oxidant. Additionally, particle counts were conducted. Results show that the application of an oxidant increased the number of smaller particles present alter settling However, this immense of particles did not significantly alter settled turbidity levels. / Master of Science

In this study, the effects of organics removal efficiency, oxidant dose, and alum dose on aluminum hydroxide sludge characteristics were assessed. In order to maintain control over operating parameters, a continuous-flow laboratory-scale plant was operated in the laboratory with daily monitoring of pH, as well as influent and effluent turbidity, total organic carbon, and color. Sludge thickening and dewatering characteristics were found to worsen when increasing amounts of organic matter were incorporated into the sludge floe matrix. Sludge properties improved with increases in oxidant dose and decreases in alum dose and alum/influent turbidity ratio. Changes in coagulation mechanism from sweep to charge neutralization were hypothesized to be partially responsible for changes in sludge properties caused by changing alum dose. Improvements in thickening and dewatering characteristics were found to be heavily dependent upon increases in sludge floe density, as well as decreases in aggregate water content. / M.S.

The objectives were to evaluate permanganate and chlorine dioxide as preoxidants both when they were dosed individually and when they were dosed together, for their abilities to improve water treatment plant performance. The specific goals were to determine the effect of the preoxidant conditions on coagulant requirements, filter operation, and the removals of organic carbon, trihalomethane precursors, iron, and manganese. Also, the interaction of the preoxidants with each other when dosed together was investigated. The preoxidant conditions were evaluated on both plant- and laboratory-scale bases. The plant-scale study focused on the ability of the preoxidants to enhance those aspects of plant performance listed above. The laboratory-scale study reinforced the results of the plant-scale study and included investigations to the interactions between the two oxidants when they were dosed simultaneously. The plant-scale study yielded information regarding the extent to which these oxidants helped remove the raw water constituents listed previously. The laboratory-scale study expanded on these results and included information concerning the reasons why these oxidants performed in the manner that they did. During the period of lake stratification, when trihalomethane removal caused the greatest treatment concerns, chlorine dioxide provided the greatest removal efficiency (65 percent), but organic carbon removal suffered (45 percent), While the lake was mixing and reduced manganese posed the greatest treatment concerns, the simultaneous use of chlorine dioxide and permanganate resulted in the greatest removal efficiency (95 percent), however, objectionable tastes-and-odors were formed. In comparison, chlorine dioxide was more apt to oxidize organic compounds (including trihalomethane and taste-and-odor precursors), and permanganate was more apt to oxidize manganese(II). When the two oxidants were dosed simultaneously, chlorine dioxide had the capacity to maintain permanganate for extended periods, possibly beyond the hydraulic retention time of the plant. Methods were developed to measure 1) chlorite concentrations in the presence of oxidized forms of manganese and 2) the relative sizes and shapes of molecular—size distributions of naturally occurring organic matter. / Ph. D.

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 critical overview document (COD) presents, discusses and brings together the selected portfolio of publications that the author believes make a significant contribution to the field of wastewater treatment, focusing on the removal of endocrine disrupting chemicals (EDCs) in wastewater treatment applications. The aim of the research within this COD was to investigate the fate, mechanisms and optimisation of EDCs removal in wastewater treatment applications. The key objectives were to: 1. Investigate and understand the mechanisms of removal of EDCs in wastewater and sludge treatment processes. 2. Evaluate novel methods for the removal of EDCs in water and wastewater treatment applications. 3. Establish the kinetic and thermodynamic properties of the removal processes to inform process modelling of full scale design of treatment processes.

In the waste management system of Peru, there is a lot to fix, change and improve from households areas. In this report is presented why and how necessary is the construction of landfills to have an appropriate place to dispose the waste of the collection .At the same time, the report shows how profitable can be from social, economic and ecologic way, with the investment of treatment plants that use biogas from the landfills to produce energy. Differents solutions – vehicle fuel production, electricity generation etc – are discussed in light of the different economy, geography and social situation in three selected cases.