930 resultados para Slow sand filters


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The application of sand filters in localized irrigation systems is recommended in the presence of organic and algae contamination. The proper design and maintenance of these equipments are essential to assure an effective water quality control, in order to reduce the emitters clogging, to keep its water application uniformity, and to prevent increasing in the system operation costs. Despite the existence of some references about design, operation and maintenance of these filters, they are dispersed, with not enough details to guarantee the optimization of its hydraulics structure design and the proper selection of porous media to be used. Therefore, the objective of this work was to report a current literature review, relating practical information with scientific knowledge. The content of this review would help to induce and intensify the research on this subject and to contribute so the operational functions for the equipment are reached. It is also expected to assist the improvement of the filtration and flushing processes in the agricultural irrigation and the development of original design procedures and the rational use of these devices.

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The aim of this study was to verify the influence of the apparent molecular size of aquatic humic substances on the effectiveness of coagulation with ferric chloride. Coagulation-filtration tests using jar test and bench-scale sand filters were carried out on samples of water with true color of approximately 100 Hazen units, prepared with aquatic humic substances of different molecular sizes (F1: < 0.45 µm, F2: 100 kDa - 0.45 µm, F3: 30 - 100 kDa and F4': < 30 kDa). For the water samples with lower apparent molecular size fractions, greater dosages of coagulant was needed to remove the color around 5.0 Hanzen units, mainly because these water samples contain higher concentrations of fulvic acids, which exhibited a larger number of negatively-charged groups.

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Um dos objetivos desta dissertação de mestrado foi avaliar o impacto ambiental do processo de tingimento usado na indústria de curtumes, em termos de volume de efluente produzido e sua carga poluente. Pretendeu-se também encontrar alternativas ao nível do processo de tingimento que levem a uma melhoria na qualidade do efluente produzido. Outro objetivo deste trabalho foi avaliar o funcionamento da ETAR existente na empresa JR Fontes, no que diz respeito aos parâmetros em estudo (carência química de oxigénio - CQO, pH, crómio e teor de sólidos suspensos totais - SST), propondo alterações que permitam respeitar os valores de emissão exigidos na licença de descarga da empresa. Verificou-se que o processo de tingimento aplicado pela empresa JR Fontes é muito poluente, em termos de carga orgânica e matéria em suspensão. Este facto é comprovado pelos resultados obtidos para os três processos estudados: Montana, Galáctico e Navak. Todos os processos apresentam um efluente com pH ácido (aproximado a 3) e valores de CQO superiores a 3550 mg O2/L, sendo o processo Navak aquele que apresenta o valor mais alto para o banho composto, 8362 mg O2/L. Relativamente ao teor de crómio, o banho de recurtume com concentração mais elevada de crómio total é o banho 1 do processo Navak, com 2297 mg/L, sendo que a concentração destes banhos é sempre elevada, igual ou superior a 746 mg/L. No que diz respeito à matéria em suspensão, o processo Navak é novamente o mais poluente, com um valor de 3842 mg SST/L, não sendo obtidos nos outros processos, valores inferiores a 1205 mg SST/L. Na realização de um processo alternativo de tingimento verificou-se que é possível diminuir a carga orgânica do efluente originado. A aplicação de recurtumes sintéticos deu origem a efluentes menos poluentes. O melhor valor obtido para a CQO foi de 1113 mg O2/L, sendo obtidos valores não superiores a 7185 mg O2/L para processos de características semelhantes aos aplicados nesta indústria. Relativamente à ETAR, apesar das restrições ao funcionamento que esta apresenta, no geral pode ser considerada eficiente, embora não consiga atingir o objetivo pretendido de remoção para a CQO, ou seja o valor de 1100 mg O2/L. Nos restantes parâmetros é cumprido o limite de emissão (350 mg SST/L, pH entre 6 e 9 e 2 mg Cr/L para o crómio total): os SST apresentam o valor de 98 mg SST/L, o crómio total de 1,2 mg Cr/L e o pH encontra-se entre 8 e 9. São aqui feitas duas abordagens para solucionar os problemas existentes na ETAR. A primeira considera um ajuste no tratamento e equipamentos existentes, através da reconstrução do tanque de equalização, da substituição do coagulante por sulfato ferroso e da reconstrução do sedimentador, assim como a substituição das tubagens por umas de maior diâmetro, solucionando assim problemas de manutenção de toda a instalação e do incumprimento da legislação. A outra abordagem implica a substituição do sistema de afinação existente, os filtros de areia e carvão ativados, por um sistema de membranas de ultrafiltração ou por dois filtros de carvão ativado. Para tratar um efluente com um valor de CQO de 3000 mg O2/L com o carvão estudado, seriam necessários 132 kg de carvão por coluna, aproveitando-se os equipamentos existentes. No caso das membranas filtrantes, estas são eficazes, reduzindo a CQO em cerca de 70%. Ao contrário do carvão, a aplicação deste sistema implicaria a aquisição de novos equipamentos. Futuramente propõe-se a avaliação dos vários tipos de reagentes usados no tingimento de couro de forma a aplicar no tratamento aqueles que produzam as características desejadas no produto final e a que apresentem um menor resultado de CQO. Propõe-se também o estudo de viabilidade da remoção de crómio dos banhos de recurtume e consequente avaliação da aplicabilidade de um tratamento biológico em substituição ou como complemento do tratamento existente.

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Este trabajo final de carrera se basa en la redacción de un proyecto de ejecución de una zona lúdica situada en el interior del recinto de un camping, la cual estará formada por una piscina de grandes dimensiones formada por tres vasos de tipo desbordante, una piscina de tipo infantil, un jacuzzi y finalmente un edificio de servicios complementarios (bar, aseos y enfermería). La piscina grande estará formada por tres vasos donde el agua va deslizándose de uno a otro hasta ser recogida por un depósito de compensación desde donde se realizará la filtración y tratamiento antes de ser devuelta al piscina de nuevo. La instalación está también preparada para ser utilizado cada vaso como una piscina individual, recogiendo el agua por los rebosaderos laterales y conduciéndola al mismo vaso de compensación. El tratamiento del agua se realizará de forma física a través de la filtración mediante filtros de arena y de forma química analizando la cantidad de cloro residual y el nivel de PH y posteriormente añadiendo de forma automática las cantidades de cloro y corrector de PH adecuados mediante bombas dosificadoras de precisión. La piscina infantil es de pequeñas dimensiones y esta preparada para ser utilizada por niños de muy corta edad. Se diferencia de la piscina grande en el sistema de recirculación de agua (en este casos e utilizarán skimmers) y en el tratamiento posterior, ya que se utilizará el sistema de hidrólisis salina para su desinfección en lugar de añadir directamente cloro. Este sistema de tratamiento del agua no es tan agresivo como el tradicional, siendo cada vez mas utilizado en piscinas de mediano y pequeño tamaño. El jacuzzi es de grandes dimensiones, disponiendo de su propio sistema de tratamiento de agua, utilizando el sistema de hidrólisis salina como en el caso de la piscina infantil. El edificio de servicios dispone de zonas de bar, enfermería y aseos. Se ha descrito desde la estructura a las instalaciones, justificando las conclusiones a través de los cálculos correspondientes, bien de forma manual, bien utilizando diverso software especializado.

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Kirjallisuusosassa käsitellään paperi- ja kartonkikoneiden eri vesijärjestelmiä, vedenkäytön vähentämistä ja sen vaikutusta prosessiin. Mikrobiologiaa, mikrobien aiheuttamia prosessiongelmia, mikrobien torjuntaa ja simulointia on myös käsitelty kirjallisuusosassa. Kokeellisessa osassa laadittiin Kartonkikone 1:n massa- ja vesijärjestelmän mikrobiologisen puhtauden simulointimalli Balas-prosessisimulointiohjelmalla. Kartongin mikrobiologinen puhtaus määritettiin kokonaispesäkelukuna. Kokeellinen osa sisälsi pilot-mittakaavan suodatinkoeajoja, joissa määritettiin tarvittavat erotusparametrit simulointimallille, selvitettiin Dynasand-hiekkasuodattimen soveltuvuus suihkuvesien puhdistukseen, Dynadisc-kiekkosuodattimen käyttökelpoisuus kiertoveden puhdistukseen kiertovesisuodattimena ja hiekkasuodattimien esisuodattimena sekä UV-reaktorin soveltuvuus suodatettujen vesien desifiointiin. Simulointimallilla tarkasteltiin eri prosessivaihtoehtojen vaikutus kartongin mikrobiologiseen puhtauteen. Suihkuvesien puhdistaminen hiekkasuodattimilla alentaa kokonaispesäkelukua vain vähän. Koneen ajettavuus paranee suihkuputkien roskaryöppyjen ja viiraosan limoittumisen vähenemisen takia. Kiertovesijärjestelmän pelkkä jakaminen hylkyprosessi- ja sakeudensäätövedeksi aiheuttaa kokonaispesäkeluvun kasvun prosessista poistettavien vesien puhdistumisen takia. Kokonaispesäkeluku minimoidaan poistamalla ylimääräinen vesi hylkysaostajan suodoksena. Suodatettua hylkysaostajan suodoksen ja viiraveden seosta käytetään sekä sakeudensäätö- että hylkyprosessivedeksi. Hylkymassalla on dominoiva vaikutus kokonaispesäkelukuun. Suurin vähennys kokonaispesäkeluvussa saadaan estämällä mikrobikasvu hylkymassassa. Tämä voidaan tehdä kuumentamalla hylkymassa 80 °C:n höyryllä. Suodatuskoeajojen perusteella Dynasand-hiekkasuodattimella voidaan puhdistaa pisaralämmönvaihtimelta saatavaa lämmintä suihkuvettä. Esisuodatettua kiertovettä voidaan puhdistaa Dynasand-hiekkasuodattimella viiran johtotelojen suihkuvedeksi. Dynadisc-kiekkosuodatinta voidaan käyttää hiekkasuodattimen esisuodattimena ja kiertovesisuodattimena. UV-säteily poistaa tehokkaasti mikrobeja suodatetuista vesistä.

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The aim of this study was to verify the influence of the apparent molecular size of aquatic humic substances on the effectiveness of coagulation with ferric chloride. Coagulation-filtration tests using jar test and bench-scale sand filters were carried out on samples of water with true color of approximately 100 Hazen units, prepared with aquatic humic substances of different molecular sizes (F1: < 0.45 µm, F2: 100 kDa - 0.45 µm, F3: 30 - 100 kDa and F4': < 30 kDa). For the water samples with lower apparent molecular size fractions, greater dosages of coagulant was needed to remove the color around 5.0 Hanzen units, mainly because these water samples contain higher concentrations of fulvic acids, which exhibited a larger number of negatively-charged groups.

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Eutrophication caused by anthropogenic nutrient pollution has become one of the most severe threats to water bodies. Nutrients enter water bodies from atmospheric precipitation, industrial and domestic wastewaters and surface runoff from agricultural and forest areas. As point pollution has been significantly reduced in developed countries in recent decades, agricultural non-point sources have been increasingly identified as the largest source of nutrient loading in water bodies. In this study, Lake Säkylän Pyhäjärvi and its catchment are studied as an example of a long-term, voluntary-based, co-operative model of lake and catchment management. Lake Pyhäjärvi is located in the centre of an intensive agricultural area in southwestern Finland. More than 20 professional fishermen operate in the lake area, and the lake is used as a drinking water source and for various recreational activities. Lake Pyhäjärvi is a good example of a large and shallow lake that suffers from eutrophication and is subject to measures to improve this undesired state under changing conditions. Climate change is one of the most important challenges faced by Lake Pyhäjärvi and other water bodies. The results show that climatic variation affects the amounts of runoff and nutrient loading and their timing during the year. The findings from the study area concerning warm winters and their influences on nutrient loading are in accordance with the IPCC scenarios of future climate change. In addition to nutrient reduction measures, the restoration of food chains (biomanipulation) is a key method in water quality management. The food-web structure in Lake Pyhäjärvi has, however, become disturbed due to mild winters, short ice cover and low fish catch. Ice cover that enables winter seining is extremely important to the water quality and ecosystem of Lake Pyhäjärvi, as the vendace stock is one of the key factors affecting the food web and the state of the lake. New methods for the reduction of nutrient loading and the treatment of runoff waters from agriculture, such as sand filters, were tested in field conditions. The results confirm that the filter technique is an applicable method for nutrient reduction, but further development is needed. The ability of sand filters to absorb nutrients can be improved with nutrient binding compounds, such as lime. Long-term hydrological, chemical and biological research and monitoring data on Lake Pyhäjärvi and its catchment provide a basis for water protection measures and improve our understanding of the complicated physical, chemical and biological interactions between the terrestrial and aquatic realms. In addition to measurements carried out in field conditions, Lake Pyhäjärvi and its catchment were studied using various modelling methods. In the calibration and validation of models, long-term and wide-ranging time series data proved to be valuable. Collaboration between researchers, modellers and local water managers further improves the reliability and usefulness of models. Lake Pyhäjärvi and its catchment can also be regarded as a good research laboratory from the point of view of the Baltic Sea. The main problem in both of them is eutrophication caused by excess nutrients, and nutrient loading has to be reduced – especially from agriculture. Mitigation measures are also similar in both cases.

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A qualidade da água é muito importante para irrigação por gotejamento, pois ela escoa por pequenos bocais dos emissores, podendo ocorrer obstrução devido à deposição dos sólidos em suspensão. Portanto, antes da instalação do projeto, devem-se avaliar parâmetros de qualidade da água, para adotar medidas preventivas, evitando o risco de entupimento do sistema. Este trabalho teve como objetivo avaliar um sistema composto por aeradores com aspersores, sobre leito de pedra, para a precipitação dos íons Fe+2e Mn+2 em tanque de decantação, e um conjunto de filtragem composto por três filtros de areia e um de disco, em sistema de irrigação localizada. O trabalho foi realizado na Fazenda Alvorada, no município de Nova Granada - SP, no período de março a outubro de 2008. Foram realizadas determinações de variáveis físicas e químicas da água, ao longo do sistema de aeração, decantação e filtragem, o qual foi eficiente para a melhoria da qualidade de água, reduzindo os níveis de risco de entupimento de severo para médio e de médio para baixo. Oxigênio dissolvido, condutividade elétrica, pH, Fe+2e Fe+3 não diferenciaram a qualidade de água entre os pontos do sistema de tratamento, porém a turbidez, sólidos dissolvidos, sólidos em suspensão, ferro total e manganês total reduziram-se significativamente pelo uso do sistema proposto, melhorando a qualidade da água.

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In this research it was studied a system composed by the anaerobic filter combined with a sand filter for the wastewater treatment. For this, three anaerobic filters were operated with hydraulic detention time of nine hours which had the effluent disposed over four sand filters in different frequencies of application. on the first sand filter, 50 L.m(-2) were applied once a day. on the second, the third and the fourth filters, the same load was disposed in twice, three and four times a day, distributed between 9 a. m. and 4 p. m. The system presented a final effluent suitable for the COD and BOD legislation maximum limit to be discharged into water body (Decreto Paulista no 8,468/1976), showing the viability of dispose a higher quantity of effluent then the one suggested by NBR 13969/1997, which guides the constructive aspects for this kind of treatment.

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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

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Today , Providing drinking water and process water is one of the major problems in most countries ; the surface water often need to be treated to achieve necessary quality, and in this way, technological and also financial difficulties cause great restrictions in operating the treatment units. Although water supply by simple and cheap systems has been one of the important objectives in most scientific and research centers in the world, still a great percent of population in developing countries, especially in rural areas, don't benefit well quality water. One of the big and available sources for providing acceptable water is sea water. There are two ways to treat sea water first evaporation and second reverse osmosis system. Nowadays R.O system has been used for desalination because of low budget price and easily to operate and maintenance. The sea water should be pretreated before R.O plants, because there is some difficulties in raw sea water that can decrease yield point of membranes in R.O system. The subject of this research may be useful in this way, and we hope to be able to achieve complete success in design and construction of useful pretreatment systems for R.O plant. One of the most important units in the sea water pretreatment plant is filtration, the conventional method for filtration is pressurized sand filters, and the subject of this research is about new filtration which is called continuous back wash sand filtration (CBWSF). The CBWSF designed and tested in this research may be used more economically with less difficulty. It consists two main parts first shell body and second central part comprising of airlift pump, raw water feeding pipe, air supply hose, backwash chamber and sand washer as well as inlet and outlet connections. The CBWSF is a continuously operating filter, i.e. the filter does not have to be taken out of operation for backwashing or cleaning. Inlet water is fed through the sand bed while the sand bed is moving downwards. The water gets filtered while the sand becomes dirty. Simultaneously, the dirty sand is cleaned in the sand washer and the suspended solids are discharged in backwash water. We analyze the behavior of CBWSF in pretreatment of sea water instead of pressurized sand filter. There is one important factor which is not suitable for R.O membranes, it is bio-fouling. This factor is defined by Silt Density Index (SDI).measured by SDI. In this research has been focused on decreasing of SDI and NTU. Based on this goal, the prototype of pretreatment had been designed and manufactured to test. The system design was done mainly by using the design fundamentals of CBWSF. The automatic backwash sand filter can be used in small and also big water supply schemes. In big water treatment plants, the units of filters perform the filtration and backwash stages separately, and in small treatment plants, the unit is usually compacted to achieve less energy consumption. The analysis of the system showed that it may be used feasibly for water treating, especially for limited population. The construction is rapid, simple and economic, and its performance is high enough because no mobile mechanical part is used in it, so it may be proposed as an effective method to improve the water quality and consequently the hygiene level in the remote places of the country.

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OBJECTIVE: Blood-sucking arthropods' salivary glands contain a remarkable diversity of antihemostatics. The aim of the present study was to identify the unique salivary anticoagulant of the sand fly Lutzomyia longipalpis, which remained elusive for decades. METHODS AND RESULTS: Several L. longipalpis salivary proteins were expressed in human embryonic kidney 293 cells and screened for inhibition of blood coagulation. A novel 32.4-kDa molecule, named Lufaxin, was identified as a slow, tight, noncompetitive, and reversible inhibitor of factor Xa (FXa). Notably, Lufaxin's primary sequence does not share similarity to any physiological or salivary inhibitors of coagulation reported to date. Lufaxin is specific for FXa and does not interact with FX, Dansyl-Glu-Gly-Arg-FXa, or 15 other enzymes. In addition, Lufaxin blocks prothrombinase and increases both prothrombin time and activated partial thromboplastin time. Surface plasmon resonance experiments revealed that FXa binds Lufaxin with an equilibrium constant ≈3 nM, and isothermal titration calorimetry determined a stoichiometry of 1:1. Lufaxin also prevents protease-activated receptor 2 activation by FXa in the MDA-MB-231 cell line and abrogates edema formation triggered by injection of FXa in the paw of mice. Moreover, Lufaxin prevents FeCl(3)-induced carotid artery thrombus formation and prolongs activated partial thromboplastin time ex vivo, implying that it works as an anticoagulant in vivo. Finally, salivary gland of sand flies was found to inhibit FXa and to interact with the enzyme. CONCLUSIONS: Lufaxin belongs to a novel family of slow-tight FXa inhibitors, which display antithrombotic and anti-inflammatory activities. It is a useful tool to understand FXa structural features and its role in prohemostatic and proinflammatory events.

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The basic concepts of digital signal processing are taught to the students in engineering and science. The focus of the course is on linear, time invariant systems. The question as to what happens when the system is governed by a quadratic or cubic equation remains unanswered in the vast majority of literature on signal processing. Light has been shed on this problem when John V Mathews and Giovanni L Sicuranza published the book Polynomial Signal Processing. This book opened up an unseen vista of polynomial systems for signal and image processing. The book presented the theory and implementations of both adaptive and non-adaptive FIR and IIR quadratic systems which offer improved performance than conventional linear systems. The theory of quadratic systems presents a pristine and virgin area of research that offers computationally intensive work. Once the area of research is selected, the next issue is the choice of the software tool to carry out the work. Conventional languages like C and C++ are easily eliminated as they are not interpreted and lack good quality plotting libraries. MATLAB is proved to be very slow and so do SCILAB and Octave. The search for a language for scientific computing that was as fast as C, but with a good quality plotting library, ended up in Python, a distant relative of LISP. It proved to be ideal for scientific computing. An account of the use of Python, its scientific computing package scipy and the plotting library pylab is given in the appendix Initially, work is focused on designing predictors that exploit the polynomial nonlinearities inherent in speech generation mechanisms. Soon, the work got diverted into medical image processing which offered more potential to exploit by the use of quadratic methods. The major focus in this area is on quadratic edge detection methods for retinal images and fingerprints as well as de-noising raw MRI signals

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This paper evaluates the efficiency of geotextile filters for sludge from a compact water treatment plant (WTP). The key aspects required in the methodology of selection and designing geotextile filters for sludge from dewatering was investigated based on laboratory tests results. The analyses were supported by the measured filtrated volume of water and turbidity resulting from variable head permeability tests carried out in two geotextiles and using the conventional granular filter (sand and gravel). The results of the present study showed that more than 75% of the dewatering sludge can be filtrated with low turbidity, which permits that this water can return to the treatment plan in order to be reuse in another cycle. The reduced volume of sludge retained by the geotextile that is transferred to the drying pound increases its efficiency by reducing the drying time. The low volume of the dry waste can be removed and the geotextile can be easily cleaned or replaced when needed. These procedures significantly reduce the volume of water needed in dewatering and also avoids waste discharges in the environment.