Este trabalho teve por objetivo estudar a desinfecção seqüencial cloro-radiação ultravioleta e ozônio-radiação ultravioleta a fim de avaliar a resistência de microrganismos indicadores de poluição fecal - E. coli, coliformes totais e Clostridium perfringens - e compará-la à dos protozoários patogênicos: Giardia spp. e Cryptosporidium spp.. Houve, primeiramente, monitoramento do reator anaeróbio UASB cujo efluente foi utilizado neste estudo. Foi, então, verificado o comportamento das espécies residuais de cloro no esgoto e conduzido um estudo de parâmetros indicadores (pH, potencial de oxi-redução e condutividade) para o breakpoint. Na desinfecção, foram empregados o cloro, ozônio e radiação ultravioleta; separados, e seqüencialmente. Os ensaios realizados com ozônio promoveram remoção de DQO, sólidos e dos valores de absorbância em 254 nm, diferentemente do cloro. A ordem crescente de resistência à desinfecção foi: E. coli < coliformes totais < C. perfringens < protozoários. Houve correlação em alguns ensaios entre a bactéria esporulada C. perfringens e Giardia spp.. O efeito sinérgico, promovido pela desinfecção seqüencial, foi evidenciado em alguns experimentos para C. perfringens e Giardia spp. / The present dissertation reports on the study of the sequential disinfection with chlorine-ultraviolet radiation and ozone-ultraviolet radiation to evaluate the resistance of microorganisms that indicate fecal pollution - E. coli, total coliforms and Clostridium perfringens - and compare it to the resistance of pathogenic protozoa: Giardia spp. and Cryptosporidium spp.. Firstly, the UASB reactor, whose effluent was utilized in this study, was monitored. Then the behavior of the residual species of chlorine in the sanitary sewage was verified and a study of the indicating parameters (pH, oxi-reduction potential and conductivity) for the breakpoint was conducted. Chlorine, ozone and ultraviolet radiation were used separately and sequentially in the disinfection. Tests performed with ozone promoted removal of COD, solids and absorbance values of 254 nm, differently from chlorine. The order of resistance to disinfection was: E. coli < total coliforms < Clostridium perfringens < protozoa. There was a correlation in some tests between spore-forming bacterium Clostridium perfringens and Giardia spp.. The synergic effect caused by the sequential disinfection was observed in some experiments for C. perfringens and Giardia spp.

PBDEs were detected in all air and dust samples. The PBDE congener profile in both outdoor and indoor air samples from Thai e-waste storage facilities and homes was dominated by BDE-47 and 99, whilst the predominant BFRs in all dust samples from Thai e-waste storage facilities were BDE-209, BDE-208, BDE-207, BDE-206, BDE-197, BDE-183, BDE-99, BDE-47 and DBDPE. Furthermore, BDEs 99 and 47 were the most abundant congeners in all dust samples from Thai houses and cars and UK homes. Under realistic high-end scenarios of occupational exposure to BDE-99 via dust ingestion, workers in Thai e-waste storage facilities were exposed above a recently-published Health Based Limit Value for this congener. For non-occupational exposure, under a high-end exposure scenario, the exposure to BDE-99 of such Thai children via dust ingestion is either very close to or in exceedance of the HBLV. PBDE levels in most of the areas monitored within the same rooms were not statistically significantly different. Similarly, concentrations of PBDEs in the majority of rooms within the same houses were not statistically significantly different between rooms. Possible dilution of PBDE levels in dust with increasing dust loadings has been identified in a small number of rooms.

Excess Fluoride in drinking water is a cause for concern in several countries in the world. Various techniques have been developed to mitigate the harmful effects of fluoride. In the present work, a combined alum and activated alumina (AA) process has been investigated. Tap water with sodium fluoride dissolved in it to produce a solution having a fluoride concentration of 5 mg/L was used as the feed. It was found that pretreatment with alum extends the time required for the regeneration of the AA column. The volume of water treated increased by 89% compared to AA process alone. Though the regeneration of the AA column has been well documented, subtle issues have ot been reported. The disposal of regeneration effluent is a concern in adsorption-based processes. This study aims to examine some of the issues involved in the regeneration of the AA column such as disposal of effluent, and the quantity of acid and alkali required. The regeneration effluent from the combined process, which had a fluoride concentration of 10-16 mg/L was treated in a solar still. The distillate from the still had a fluoride concentration of 2-3 mg/L, which is much lower than the concentration of the regeneration effluent. The cost of treatment decreased with each regeneration cycle and after four regenerations the cost was Rs 0.5/L of treated water. The volume of water treated after four regenerations was 307 L/Kg of AA. Studies were also done using field water from Banavara, Hassan district, Karnataka, which had a fluoride concentration of 3,0-3.5 mg/L. The combined process successfully produced treated water having an acceptable fluoride concentration. After one regeneration cycle, the operating cost was Rs. 1/L of treated water. Studies have also been conducted on a point-of-use water filter containing a bed of AA pellets. The filter was provided by an organization called TIDE. The present results appear to suggest that a column with a smaller diameter than the TIDE filter has a better removal capacity. Ceramic candles are widely used for water filtration as they are readily available and inexpensive. Hence they are suitable for household water treatment purposes. In the present work, ceramic candles have been impregnated with nano-size alumina and nano-size magnesium oxide and tested for their defluoridation capacity. The nanoparticles were generated in situ in the pores of the candle by solution combustion synthesis. It has been found the candle impregnated with nano-size magnesium oxide has a higher defluoridation capacity than nano-size alumina. Estimation of the particle size in the samples of treated water did not give conclusive evidence for the presence or absence of nanoparticles. The volume of water treated was low and the cost of treatment was high (Rs. 12/L for the candle impregnated with MgO). Hence such candles are unsuitable for defluoridation. Batch adsorption has been employed to measure the adsorption capacity of adsorbents. A model to capture the overall picture of the batch adsorption process, obtaining the kinetic and transport parameters involved has been developed. The mathematical model takes into account external mass transfer resistance, intraparticle diffusion, adsorption, and desorption. The equilibrium adsorption data was fitted using the Langmuir isotherm. The governing equations were solved using a finite difference technique known as the Laasonen method. The parameters were estimated by fitting two sets of data using a MATLAB function. The values estimated suggest that the adsorption process may not be diffusion-limited, in contrast to the assumption commonly used in the literature. The estimated parameter values were used to predict the concentration profiles for the other data sets. It was found that predicted and measured profiles agreed reasonably well.

Groundwater is a major and sometimes lone source of drinking water worldwide. The chemical composition of groundwater is a combined product of the composition of water that enters the aquifer and its reaction with various minerals present in the soil and rock mass, which alter the water composition with time and space. Some important factors influencing groundwater quality are (1) physiochemical characteristics o the rocks through which the water circulates; (2) geology of the location; (3) climate of the area; (4) role of microorganisms, which includes oxidative and reductive biodegradation of organic matter; (5)chemical, physical, and mineralogical characteristics of the overburden soils through which the rainwater percolates; and (6) human intrusion affecting the hydrological cycle and degradation in water quality through utilization of water for agricultural and industrial activities. By far the most serious naturally occurring groundwater-quality problem in India derives from high fluoride, arsenic and iron concentrations which are dissolved from the bedrocks by geochemical processes. Presence of excess fluoride in groundwater is identified as a naturally occurring health hazard by the World Health Organization (WHO). Prolonged ingestion of fluoride beyond certain permissible limit leads to ffluorosis, one of the common water-related diseases recognized by the WHO and the United Nations Children's Fund (UNICEF). Endemic fluorosis is now known to be global in scope, occurring on all continents and affecting many millions of people. According to estimates made in the early 1980s, around 260 million people in 30 countries worldwide were drinking water with more than 1 ppm of fluoride. The ultimate source of fluoride in water, soil or biosphere is associated with its distribution in rocks and its dispersion in groundwater. The three most important minerals of fluoride are fluorite (CaF2), cryolite (Na3AlF6) and fluorapatite (Ca5(PO4)3F); cryolite is a rare mineral where as by far the largest amount of fluorine in the earth's crust is in the form of fluorapatite (about 3.5% by weight of fluorine) which is processed almost exclusively for its phosphate content. Fluoride substitutes readily in hydroxyl positions in late-formed minerals in igneous rocks, and in primary minerals especially micas (such as biotites) and amphiboles (such as hornblende). The most important controlling factors influencing fluoride presence in groundwater include: distribution of easily weathered fluoride-bearing minerals, the accessibility of circulating water to these minerals, pH of the percolating water, calcium content of the leaching water, temperature of the percolating water and the soil, exchangeable ions in the percolating water, extent of fresh water exchange in an aquifer, evaporation and evapotranspiration, complexing of fluoride ions with other ions, presence of CO2 and other chemicals in draining water and residence time of the percolating water in soil. High fluoride levels are observed in the groundwater in 19 states of the country. Fluorite, apatite, rock phosphate, phosphorites, phosphatic nodules and topaz are major fluoride bearing minerals in India with varying levels of fluoride content. There are three major fluoride bearing areas in India :1) Gujarat-Rajasthan in the north-west and 2) Chandidongri-Raipur in central India 3) Tamil Nadu-Andhra Pradesh in the south; besides other areas in Karnataka, Bihar, Punjab and in the North-west Himalayas. The total mineral reserves of fluorite, rock phosphate and apatite in the country are estimated at 11.6, 71 and 2.82 million tonnes respectively. The distribution of areas with excess fluoride in groundwater concurs with that of fluorine-bearing minerals. Further high fluoride concentrations are observed from arid and semi arid regions of the country and the areas with advanced stage of groundwater development. An estimated 62 million people, including 6 million children suffer from fluorosis in India because of consuming fluoride-contaminated water. Endemic fluorosis is found to practically exist only in the villages due to lack of piped water supply. The Indian Drinking Water Standard specifies the desirable and permissible limits for fluoride in drinking water as 1.0 and 1.5ppm respectively. De-fluoridation of groundwater is the only alternative to prevent fluorosis in the absence of alternate water source especially for immediate and/or interim relief. De-fluoridation of drinking water in India is usually achieved by the Nalgonda technique or activated alumina process. The Nalgonda method involves addition of aluminum salts (aluminium sulphate and/or aluminium chloride), lime and bleaching powder to water, followed by rapid mixing, flocculation, sedimentation, filtration and disinfection. Only aluminum salt is responsible for removal of fluoride from water .Fluoride removal is achieved in a combination of complexation with polyhydroxy aluminium species and adsorption on polymeric alumino hydroxides (floc). Activated alumina(Al2O3) was proposed for de-fluoridation of water for domestic use in 1930’s and since then it has become one of the most advocated de-fluoridation methods. Activated alumina is a semi crystalline porous inorganic adsorbent and an excellent medium for fluoride removal. When the source water passes through the packed column of activated alumina, fluoride (and other components in the water) is removed via exchange reaction with surface hydroxides on alumina; this mechanism is generally called adsorption although ligand exchange is a more appropriate term for the highly specific surface reactions involved. The fluoride removal capacity of alumina is highly sensitive to pH, the optimum being about pH5.5-6. Significant reduction in fluoride removal by activated alumina is also observed in presence of sulfate and silicate ions. The column needs periodic regeneration once break point(where the effluent concentration is, for example, 2ppm at normal saturation) is reached. For regeneration, the medium is backwashed for 5-10 min and then subjected to two step regeneration with base (NaOH) followed by acid(H2SO4). A major cause for concern with the Nalgonda method is the possibility of formation of residual aluminum and soluble aluminum fluoride complexes in the treated water and a potential breach of the 0.2ppm Indian drinking water standard for aluminium. Concerns with the activated alumina filter method are that the process is pH dependent, with an optimum (pH) working range of 5-6. Further, the activated alumina column requires periodic recharge using caustic soda and acid solutions to rejuvenate the fluoride retention capacity of the column. After 3-4 regenerations the medium has to be replaced. If the pH is not readjusted to normal following the regeneration process, there is a possibility that the aluminum concentration in the treated water may exceed the 0.2ppm standard. Due to the aforementioned drawbacks of the currentde-fluoridation technologies in India that chiefly rely on aluminum based compounds, magnesia(magnesium oxide, MgO) is selected to develop an alternate sustainable de-fluoridation method. The potential of MgO for de-fluoridation has been examined owing to its very limited solubility(6.2mg/L), non-toxicity and excellent fluoride retention capacity. A review of the previous studies on fluoride removal using MgO reveals that the relevant information is essentially scattered. Though studies demonstrated the fluoride removing ability of MgO and brought into focus certain aspects of the fluoride removal mechanism and change in water quality upon MgO addition, vital issues necessary for efficient design and successful field implementation of the de-fluoridation processusing MgO were not addressed. The significant limitations in the earlier works include: influence of process variables(such as MgO dosage, initial fluoride concentration, contact time, temperature, initial solution pH, presence of co-ions and ionic strength) on fluoride retention characteristics (such as removal rate, equilibrium time, capacity) of MgO were not systematically determined, optimum operating parameters/conditions (such as MgO dosage, stirring and settling time) for effective de-fluoridation process applicable to a wide range of groundwater chemical composition and fluoride concentrations were not defined, mechanism of fluoride retention by MgO was not fully understood, issue of lowering the pH of MgO treated water within potable water limits was not comprehensively addressed, safe disposal methods of fluoride bearing sludge were not explored. Failure to address the above issues has impeded the adoption of the MgO treatment method for fluoride removal from water. Scope of the study Present study aims to develop a new sustainable de-fluoridation method, applicable to a wide range of groundwater chemical compositions and fluoride concentrations, based on co-precipitation/precipitation-sedimentation-filtration processes using light MgO. Efforts are made to implement the method at domestic level in a rural area with incidence of high fluoride concentration in groundwater and to understand the status and geochemistry of fluoride contamination in the area. The main objectives of the study include: To determine the fluoride retention characteristics of MgO viz.,rate, equilibrium time and capacity of fluoride retention. To examine the influence of process variables on fluoride retention characteristics of MgO and to determine the optimum operating parameters for effective de-fluoridation process. To understand the mechanism and rate limiting step of MgO de-fluoridation process. To propose methods and specifications to lower the pH of MgO treated water within permissible limits to ensure its potability. To design a simple to use, single-stage domestic de-fluoridation unit. To propose procedures for implementation of the new de-fluoridation method in field. To evaluate the efficiency of the new de-fluoridation method as a useful remedial measure in the fluoride affected areas. To understand the geochemical factors governing the quality of the fluoride rich groundwater and to ascertain the status and geochemistry of fluoride contamination in the area where felid implementation of de-fluoridation method is planned. To characterize the fluoride bearing sludge and propose methods for safe disposal and reuse of fluoride bearing sludge. Organization of the thesis Chapter1 presents an overview of the various aspects of excess fluoride presence in groundwater, remedial measures, and emphasizes the need for a new sustainable de-fluoridation method and defines the scope of present study. Chapter 2 performs a detailed investigation to determine the fluoride retention characteristics of MgO under the influence of various process variables at transient and equilibrium conditions using batch studies. The process variables that have been considered are, contact time, initial fluoride concentration, dosage of MgO, temperature, initial pH, presence of co-ions and ionic strength. Studies to determine the optimum operating parameters for efficient de-fluoridation and to understand some basics of reaction mechanisms involved are also part of this chapter. Chapter 3 examines the true nature of the reaction mechanism between fluoride ions and MgO in aqueous media and the rate-limiting step of the de-fluoridation process by investigating the hydration process of MgO and its influence/relation on fluoride removal. Chapter 4 addresses issues that will assist applying the MgO treatment method for fluoride removal in field such as 1)methods and specifications for lowering the pH of the MgO treated water within permissible limits, 2)design of a simple to use, single-stage de-fluoridation unit, and 3)characterization of the resultant fluoride bearing sludge. Chapter 5 performs a detailed investigation to evaluate the efficiency of the new de-fluoridation method in laboratory and field, and to understand the origin and the geochemicall mechanisms driving the groundwater fluorine enrichment in the area where field implementation of the de-fluoridation unit was planned. Chapter 6 explores an environmentally safe route for the disposal and re-use of fluoride bearing sludge in soil based building materials such as, stabilized soil blocks (produced by cement stabilization of densely compacted soil mass) which are alternative to burnt bricks. Chapter 7 summarizes the major results, observations and contributions from the study.

No description available.

Indoor air quality has become a challenge together with the global aim &lsquo / decreasing energy consumption&rsquo / . Increasing insulation levels of building envelopes but implementing inaccurate building system details has caused excessive heat, accumulation of pollutants, etc. in spaces. In terms of educational spaces, the increase in complaints and illnesses due to unfavorable indoor air conditions leads to a decrease in concentration and so academic performance of students and staff. In the context, the aim of the study was indicating the poor indoor air quality conditions caused by inadequate fresh air supply in crowded educational spaces and making recommendations for the improvement. In the study, a classroom and a design studio in the METU Faculty of Architecture building were investigated. In order to examine the existing situation, at two locations of each room the temperature, relative humidity and CO2 were continuously recorded between 13 September 2011 and 24 February 2012 and air speed for ten-day periods between 26 November 2011 and 5 January 2012. The evaluation of the collected data indicated that both of the rooms had temperature, so relative humidity and CO2 accumulation problems mainly due to insufficient fresh air supply in the winter period. In order to eliminate the poor conditions in the rooms, the needed outdoor air can be provided through the inlet openings coupled with fan coils, which are in existence but not in use.

INTRODUCCIÓN: El síndrome de Cushing (SC) representa una de esas enfermedades endocrinas raras, está caracterizada por una hipersecreción de cortisol; está causada por un tumor en la hipófisis (enfermedad de Cushing), o más raramente por un tumor adrenal o ectópico. La principal causa de morbilidad y mortalidad en el SC es la enfermedad cardiovascular, incluso si los pacientes han sido tratados de manera eficaz (es decir, se ha controlado el hipercortisolismo). A pesar de las múltiples complicaciones que pueden sufrir los pacientes con SC y de la presencia de numerosos factores de riesgo cardiovascular (obesidad central, diabetes, cardiopatía isquémica, hipertensión, dislipemia, etc.) potencialmente peligrosos, no existen en la actualidad programas educativos que den respuesta a este déficit formativo. Para el paciente con SC no existe hasta ahora una atención integral que permita afrontar la complejidad de esta enfermedad y conseguir una mejora de la Calidad de Vida, la disminución en la morbi-mortalidad, el aumento del confort, bienestar y autonomía en el autocuidado Dicho aspecto permite que enfermería se situé en primera línea de actuación frente a la educación en este grupo de pacientes, a través de la elaboración y el fomento de instrumentos educativos específicos que mejoren la Calidad de vida de estos pacientes. OBJETIVOS GENERALES: Evaluar la efectividad de las sesiones educativas para los pacientes con Síndrome de Cushing operados y con seguimiento ambulatorio en el HSCSP y Hospital Clínico de Barcelona, en términos de calidad de vida, indicadores de evaluación clínica, nivel de dolor y actividad física, patrones de descanso y consumo de recursos sanitarios (seguimiento realizado entre 2010 y 2011). DISEÑO,ÁMBITO Y SUJETOS DE ESTUDIO: Se realizo un ensayo clínico Multicentrico, prospectivo, con asignación aleatoria y estratificada por centros. El ámbito de estudio se desarrollo en dos centros de referencia de Cataluña donde atienden a pacientes afectados de Síndrome de Cushing (SC), uno es el Hospital de la Santa Creu i Sant Pau (HSCSP) y el Hospital Clínico de Barcelona. La muestra final fue de 61 pacientes RECOGIDA Y ANÁLISIS DATOS: La recogida de datos se realizo a través de la Historia Clínica del paciente y analizamos variables sociodemográficas, antropométricas, analíticas y clínicas y relacionadas con el SC a lo largo de todas las sesiones educativa. Así mismo se pasaran cuestionarios al inicio y al finalizar las sesiones educativas y fueron: Calidad CushingQoL, Cuestionario Internacional Physical Activity Questionnaire (IPAQ), Cuestionario Oviedo del sueño (COS), Fagerström Test for Nicotina Dependence (FTND), Cuestionario del dolor Español (CDE), Test Diagnóstico para la Disfunción Eréctil (IIDE 5), Cuestionario sobre la función sexual femenina (Spanish versión of FSFI) , Cuestionario breve perfil de la función sexual en la mujer (B-PFSF) y Cuestionario de hábitos de vida relacionados con el sobrepeso y obesidad. RESULTADOS: Se presentan mejorías significativas en el grupo intervención con respecto al grupo control en : nivel de dolor (p=0,0525), mejoría de la actividad física (p=0,0072) y hábitos de vida (p<0,0001). Así mismo se confirma asociaciones del CushingQoL con : CushingQoL basal-final (p=0,0085), mejoría del dolor (p=0,053), actividad física (p=0,0068) y nivel de descanso o sueño (p=0,0098).CONCLUSIONES: Las sesiones educativas interrumpen el deterioro de la calidad de vida, aumenta la actividad física moderada y vigoroso, favorece la adherencia al tratamiento analgésico provocando una disminución del dolor, mejora en los patrones de descanso y una disminución de los recursos consumidos en el grupo intervención. / INTRODUCTION: Cushing's syndrome (CS) is one of those rare endocrine diseases, is characterized by hypersecretion of cortisol, is caused by a pituitary tumor (Cushing's disease), or more rarely by an adrenal tumor or ectopic. The main cause of morbidity and mortality in the SC is cardiovascular disease, even if patients have been treated effectively (ie, has controlled the hypercortisolism). Despite the many complications that patients may suffer SC and the presence of several cardiovascular risk factors (central obesity, diabetes, ischemic heart disease, hypertension, dyslipidemia, etc.). Potentially dangerous, there are currently no educational programs respond to this educational deficit. For the patient with SC so far no comprehensive care that will address the complexity of this disease and achieve an improved quality of life, decreased morbidity and mortality, increased comfort, convenience and independence in self-care Said aspect allows nursing site frontline action against education in this group of patients, through the development and promotion of specific educational tools that improve the quality of life of these patients. OBJECTIVES: To assess the effectiveness of the educational sessions for patients with Cushing's syndrome and operated outpatient follow the HSCSP and Hospital Clinic of Barcelona, in terms of quality of life, clinical evaluation indicators, level of pain and physical activity, patterns of rest and use of health resources (monitoring conducted between 2010 and 2011). DESIGN, STUDY SCOPE AND SUBJECTS: We performed a multicenter, prospective, randomized, stratified by center. The field study was conducted in two reference centers in Catalonia where care for patients suffering from Cushing's syndrome (CS), one is the Hospital de la Santa Creu i Sant Pau (HSCSP) and the Hospital Clinic of Barcelona. The final sample of 61 patients DATA COLLECTION AND ANALYSIS: Data collection was performed through the patient's history and analyze sociodemographic, anthropometric, laboratory, and clinical and related SC over all educational sessions. So pass same questionnaires at the beginning and end of the educational sessions and were CushingQoL Quality, Questionnaire International Physical Activity Questionnaire (IPAQ), Oviedo Sleep Questionnaire (COS), Fagerström Test for Nicotine Dependence (FTND), Spanish Pain Questionnaire (CDE) Diagnostic Test for Erectile Dysfunction (IIEF 5), Questionnaire on female sexual function (Spanish version of FSFI) Questionnaire brief profile of female sexual function (B-PFSF) and lifestyle questionnaire related overweight and obesity. RESULTS: We present significant improvements in the intervention group compared to control group: pain level (p = 0.0525), improvement in physical activity (p = 0.0072) and lifestyle (p<0.0001). Also confirmed CushingQoL associations with: CushingQoL basal-end (p = 0.0085), improvement in pain (p = 0.053), physical activity (p = 0.0068) and level of rest or sleep (p = 0, 0098). CONCLUSIONS: The educational sessions disrupt the deteriorating quality of life, increasing moderate and vigorous physical activity, promotes adherence analgesic causing a decrease in pain, improved rest patterns and a decrease in the resources consumed in the intervention group.

Up to date, sludge filterability has been characterized by the Ruth&rsquo / s classical filtration theory and quantified by the well-known parameter specific cake resistance (SCR). However, the complexity of the actual phenomenon is clearly underestimated by the classical filtration theory and SCR is often not satisfactory in describing filterability. Although many scientific studies were conducted for a better analysis and understanding of the filtration theory, still a practically applicable solution to replace the classical theory for a better description of filterability has not been proposed yet. In the present study, blocking filtration laws proposed by Hermans and Bred&eacute / e, dating back to 1936, which have been extensively used in the membrane literature for the analysis of fouling phenomenon and the multiphase filtration theory developed by Willis and Tosun (1980) highlighting the importance of the cake-septum interface in determining the overall filtration rate have been adopted for the analysis of filterability of sludge systems. Firstly, the inadequacy of the classical filtration theory in characterizing the filterability of real sludge systems and also the lack of the currently used methodology in simulating filtration operation was highlighted. Secondly, to better understand the effect of slurry characteristics and operational conditions on filtration, model slurries of spherical and incompressible Meliodent particles were formed. Finally, a methodology was developed with the gathered filtration data to assess the filterability of the sludge systems by both theories. The results clearly show that both approaches were superior to the classical approach in terms of characterizing the filterability of sludge systems. While blocking laws yielded a slurry specific characterization parameter to replace the commonly used SCR, the multiphase theory provided a better understanding of the physical reality of the overall process.

In this study, domestic wastewater was used to determine the anaerobic treatment performances of a dilute wastewater in one-phase upflow anaerobic sludge blanket (UASB) system and two-phase upflow anaerobic filter (UAF) and UASB system. The acidification performances of domestic wastewater were compared in UAF and UASB reactors. The degree of acidification is higher in UAF reactor (31%) compared to UASB reactor (18%) at 2 h hydraulic retention time (HRT) in the anaerobic treatment of domestic wastewaters. The effluent total volatile fatty acid (tVFA) concentration was higher in UAF reactor than that the UASB reactor at 2 h HRT. The total chemical oxygen demand (tCOD) removal is 40% in winter and 53% in summer in UAF reactor at 2 h HRT. The tCOD removals in two-phase UAF and UASB system and one-phase UASB system were 83% and 63%, respectively, in 4 h HRT. The conversion rate of COD removed to methane were between 0.005 and 0.067 Nm3 methane/kg COD removed and between 0.158 and 0.233 Nm3 methane/kg COD removed in the UAF and the UASB reactor of the two-phase system, respectively. The conversion rate of COD removed to methane varied between 0.029 and 0.199 Nm3 methane/kg COD removed in one-phase UASB reactor. The results of this study showed that the two-phase reactor system consisting from UAF and UASB reactors provide a good removal of soluble organics variations in acidification reactor and better methane productions in UASB reactor at temperatures 20&deg / C and 35&deg / C through the treatment of domestic wastewater at a HRT of 4 hours.

ABSTRACT DRINKING WATER QUALITY IN ANKARA: A MONITORING STUDY Tezce, G&ouml / zde MS, Department of Environmental Engineering Supervisor: Prof. Dr. &Uuml / lk&uuml / Yetis Co-Supervisor: Prof. Dr. Filiz B. Dilek December 2010, 124 pages Following the event of severe drought experienced in 2007, it was decided to use Kesikk&ouml / pr&uuml / Reservoir as an additional source of water supply for the city of Ankara. Thereupon, there have been debates on the quality of Kesikk&ouml / pr&uuml / Reservoir water with the claims that some parameters, primarily sulfate and arsenic, were not complying with the quality standards and therefore there was a threat to public health. This study aims to determine whether the water quality in the distribution network in Ankara exceeds water quality standards, and to assess the status of water quality of Ankara. To this end, monthly samples were collected from 24 districts as distribution network water and also from the Kesikk&ouml / pr&uuml / Reservoir as source water, and were monitored in terms of certain water quality parameters during the period of July 2008 through June 2009. Sulfate concentration in Kesikk&ouml / pr&uuml / Reservoir water was measured as 300-500 mg/l and this high sulfate concentration in the source water led to high sulfate values in distribution system. On the other hand, the arsenic concentration in Kesikk&ouml / pr&uuml / water was analyzed between 9-11 &micro / g/l which is lower than the expected high arsenic concentration in Kizilirmak water. Moreover, monitoring of THM and HAA in distribution network was carried out to follow DBPs formation. The highest THM concentration was observed as 109 &micro / g/l for Bilkent in July 2008. Although for some districts and some months throughout the year THM concentration was higher than the EPA Stage-I (80 &micro / g/l) and Stage-II (40 &micro / g/l) limits, mean annual THM concentrations for districts in distribution system satisfies the standards. Furthermore, the highest HAA5 concentrations were determined as 75 &micro / g/l for Dikmen in February 2009. However, annual average HAA5 in any of the districts did not exceed USEPA limit of 60 &micro / g/l. Nonetheless, total/fecal coliform bacteria, which are the indicators of microbiological contamination, were detected in distribution system between the months of July 2008 and January 2009. However, the coliform bacteria did not appear with the increasing residual chlorine in the distribution system since January 2009. Results from this study demonstrate a temporal variability in water quality / indicating water quality deterioration in the distribution system during some months, while almost full compliance with the water quality standards during other months. Overall / due to Kesikk&ouml / pr&uuml / raw water, sulfate content appears to be the major concern in the water quality when considered the one-year monitoring period.