Biodegradation of the cyanobacterial toxin microcystin LR in natural water and biologically active slow sand filters

A bacterium (MJ-PV) previously demonstrated to degrade the cyanobacterial toxin microcystin LR, was investigated for bioremediation applications in natural water microcosms and biologically active slow sand filters. Enhanced degradation of microcystin LR was observed with inoculated (1 x 10(6) cell/mL) treatments of river water dosed with microcystin LR (> 80% degradation within 2 days) compared to uninoculated controls. Inoculation of MJ-PV at lower concentrations (1 x 10(2)-1 x 10(5)cells/mL) also demonstrated enhanced microcystin LR degradation over control treatments. Polymerase chain reactions (PCR) specifically targeting amplification of 16S rDNA of MJ-PV and the gene responsible for initial degradation of microcystin LR (mlrA) were successfully applied to monitor the presence of the bacterium in experimental trials. No amplified products indicative of an endemic MJ-PV population were observed in uninoculated treatments indicating other bacterial strains were active in degradation of microcystin LR, Pilot scale biologically active slow sand filters demonstrated degradation of microcystin LR irrespective of MJ-PV bacterial inoculation. PCR analysis detected the MJ-PV population at all locations within the sand filters where microcystin degradation was measured. Despite not observing enhanced degradation of microcystin LR in inoculated columns compared to uninoculated column, these studies demonstrate the effectiveness of a low-technology water treatment system like biologically active slow sand filters for removal of microcystins from reticulated water supplies. Crown Copyright (c) 2006 Published by Elsevier Ltd. All rights reserved.

Performance evaluation of multi-stage filtration with use of granular activated carbon and synthetic non-woven fabrics

The multi stage filtration (MSF) is an alternative that permits to enlarge the spectrum of application of the slow sand filtration as for the effluent quality and run duration. In this research the use of MSF technology associated to a granular activated carbon (GAC) column as polishing mechanism of the final effluent was evaluated; in the slow sand filters GAC was used as an intermediate layer and non-woven synthetic fabrics were utilized as a first layer of the filter media. Five different tests were conducted, where the systems subjected to the treatment were: water from the Ipe Lake (Ilha Solteira, Sao Paulo, Brazil); water from the lake with water from a recreational fish pond; water from the lake with a phytoplankton and cyanobacteria overload simulation, with and without the use of the pre-filters as a stage of the treatment. The synthetic fabrics and GAC use resulted in the best turbidity removal and an efficient apparent and true color removal; in spite that the polishing columns reported similar results for those parameters. The utilization of GAC as an intermediate layer contributed to a better organic matter removal and the fabrics improved chlorophyll-a removal. The pre-filtration columns made an efficient algae and cyanobacteria removal, a function that was completed by the filters and reached >98% efficiency. The synthetic non-woven fabrics and GAC inclusion in MSF operation improved performance of this technology with ease of application and operation.

Treatment of packinghouse wastewater by intermittent sand filtration /

Grant no. S-803766.

Studies on the removal of nematodes by rapid sand filtration /

"Supported by Federal Water Pollution Control Administration Research Project WP-00047.

Utilización de columnas verticales de filtración de manta y arena como pre-tratamiento de un sistema de filtración lenta

Slow sand filtration is an efficient water treatment technique used for treating surface water with relatively low levels of contamination. Despite the slow sand filtration at pathogen, algae and cyanobacteria removal efficiency, it has some restrictions in relation to the required area for slow filters, and the cleaning activities for the filters and the stone pre-filters when used in the treatment. This research evaluated during 120 days the use of non woven & sand pre-filtration columns as part of a slow filtration process for the apparent color, turbidity, algae, cyanobacteria, phytoflagellates and diatomaceous. The columns shown an efficient removal of the monitored parameters and demonstrated as a vantage their faster and easier cleaning process and less awkward than the required to the stone pre-filters. The turbidity removal efficiency increased progressively during the experiment, especially after the first 35 days of the start; the apparent color removal by the pre-filtration columns was of 85%, and working together with the polishing of activated carbon columns was up to 95; the diatomaceous, phytoflagellates, algae and cyanobacteria removal by the columns achieve a weekly average of 95%, its recommended to use filtration rates lower to 1,5m(3)/m(2)/d.

Remoção de substâncias húmicas por meio da oxidação com ozônio e peróxido de hidrogênio e FiME

A filtração em múltiplas etapas (FiME) se apresenta como uma alternativa para realizar o tratamento de água de comunidades de pequeno porte, entretanto, a eficiência quanto à remoção de cor verdadeira associada ao carbono orgânico dissolvido (COD) ou às substâncias húmicas, tem sido questionada ou relatada como baixa. A presente pesquisa avaliou a remoção de substâncias húmicas na FiME com pré-oxidação, com ozônio e peróxido de hidrogênio, utilizando para essa avaliação parâmetros indiretos como cor verdadeira, absorvância UV (254 nm) e COD. Foram realizados cinco ensaios, utilizando quatro filtros lentos, sendo dois com camada de carvão ativado granular (CAG). Foram ensaiadas várias alternativas de pré-oxidação com ozônio e peróxido de hidrogênio. Foram obtidos bons resultados, tendo como principal conclusão que os filtros lentos com CAG, precedidos de oxidação com ozônio e depois peróxido de hidrogênio, apresentaram remoção média de cor verdadeira de 64%, mas que o peróxido de hidrogênio afeta o desenvolvimento da camada biológica, interferindo no desenvolvimento da perda de carga, na remoção de turbidez, na remoção de coliformes e na remoção de substâncias húmicas.

Estudo da remoção do herbicida atrazina por biofiltração em filtros lentos de areia e carvão ativado associada à ação microbiana

Pós-graduação em Engenharia Civil - FEIS

Remoção de micropoluentes na filtração lenta com pré-oxidação com radiação solar

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Utilização de colunas verticais de filtração em manta e areia como pré-tratamento de filtro lento

Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

Avaliação da remoção de compostos farmacológicos em filtro ecológico seguido por filtro de carvão granular biologicamente ativado

Pós-graduação em Engenharia Civil - FEIS

Optimization of flocculation process and continuous filtration for sea water primary treatment filtration to reduce SDI for entree to reverse osmosis system

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.

Sistemas de abastecimento de água e saneamento básico

O presente relatório de estágio enquadra-se no âmbito do Trabalho Final de Mestrado (TFM) do curso de Engenharia Civil, área de especialização de Hidráulica, do Instituto Superior de Engenharia de Lisboa, e baseia-se na temática dos sistemas de abastecimento de água e drenagem de águas residuais. O estágio, intitulado de “Sistemas de Abastecimento de Agua e Saneamento Básico”, decorreu numa empresa de consultaria de engenharia denominada ENGIDRO – Estudos de Engenharia, Lda., vocacionada para a realização de estudos e projectos na área de Hidráulica, com particular incidência na Hidráulica Urbana e Saneamento Básico. O estágio iniciou-se com um adequado enquadramento profissional na empresa e incidiu principalmente no desenvolvimento de trabalhos de concepção e dimensionamento, a nível de projectos de execução, de sistemas de abastecimento de água e de saneamento básico, para 21 localidades da província de Lunda Sul, em Angola, com prestação de serviços para o Governo Provincial de Lunda Sul – Direcção Provincial da Energia e Aguas, juntamente com empresa CENGA – Consultores de Engenharia de Angola, S.A. Na prestação de serviços à entidade contratante foram efectuados trabalhos de campo, que consistiram principalmente em reconhecimentos do terreno, levantamentos topográficos e recolha de informação relevante sobre elementos condicionantes dos projectos (origens e disponibilidades de água, natureza e declive dos terrenos, tipos de infra-estruturas locais) e trabalhos de gabinete para compilação e análise da informação recolhida na elaboração dos projectos de execução, incluindo pecas desenhadas (desenhos pormenorizados) e peças escritas (memórias descritivas e justificativas, medições e orçamentos). Sendo os projectos destinados a aglomerados populacionais pouco desenvolvidos e com carências e condicionantes de diversa ordem (falta de energia eléctrica, de acessos, de telecomunicações, de meios técnicos e materiais, entre outros), prestou-se especial atenção aos aspectos da concepção, privilegiando soluções de baixa tecnologia, mais fáceis de explorar e manter com os recursos locais disponíveis.

Biodiversity of amoebae and amoebae-resisting bacteria in a drinking water treatment plant

The complex ecology of free-living amoebae (FLA) and their role in spreading pathogenic microorganisms through water systems have recently raised considerable interest. In this study, we investigated the presence of FLA and amoebae-resisting bacteria (ARB) at various stages of a drinking water plant fed with river water. We isolated various amoebal species from the river and from several points within the plant, mostly at early steps of water treatment. Echinamoeba- and Hartmannella-related amoebae were mainly recovered in the drinking water plant whereas Acanthamoeba- and Naegleria-related amoebae were recovered from the river water and the sand filtration units. Some FLA isolates were recovered immediately after the ozonation step, thus suggesting resistance of these microorganisms to this disinfection procedure. A bacterial isolate related to Mycobacterium mucogenicum was recovered from an Echinamoeba-related amoeba isolated from ozone-treated water. Various other ARB were recovered using co-culture with axenic Acanthamoeba castellanii, including mycobacteria, legionella, Chlamydia-like organisms and various proteobacteria. Noteworthy, a new Parachlamydia acanthamoebae strain was recovered from river water and from granular activated carbon (GAC) biofilm. As amoebae mainly multiply in sand and GAC filters, optimization of filter backwash procedures probably offers a possibility to better control these protists and the risk associated with their intracellular hosts

Planta pilot d'una potabilitzadora

Treball de recerca realitzat per alumnes d'ensenyament secundari i guardonat amb un Premi CIRIT per fomentar l'esperit científic del Jovent l'any 2009. El treball ha consistit en dissenyar i construir una planta pilot d'una potabilitzadora que simulés el funcionament de les plantes potabilitzadores, basada en els mateixos principis . La Planta pilot de la potabilitzadora consta de les següents operacions: desbast, floculació, decantació, filtració de sorra, aireació, filtració de carbó actiu i desinfecció. La mostra utilitzada per la potabilització s’ha obtingut de l’embassament del Pasteral, lloc on la planta potabilitzadora de Girona capta l’aigua. Una vegada potabilitzada s’han realitzat una sèrie d’anàlisis tant a l’entrada com a la sortida, per determinar la variació obtinguda en diferents paràmetres del procés. Els tipus d’anàlisis realitzats són: fisicoquímics, microbiològics i organolèptics. Finalment, s’ha realitzat una comparació amb la potabilitzadora de Girona i s’ha verificat mitjançant els paràmetres de la normativa de l’aigua l'estat de la mostra.

Jälkikäsitellyn jätevesikirkasteen uusiokäyttö Anjalan paperitehtailla

Työssä tarkasteltiin aktiivilietelaitoksen jätevesikirkasteen uusiokäyttöä Anjalan paperitehtailla. Tavoitteena oli löytää keino jätevesimäärän vähentämiseksi, kierrättämällä jatkokäsiteltyä jätevesikirkastetta. Työssä tehtiin prosessisuunnitelma kirkasteen kierrättämiseksi; suunnitelman vaikutuksia arvioitiin kirjallisuuden, simuloinnin ja arkkikokeiden avulla. Lisäksi arvioitiin kierrätyksen taloudellisia näkökohtia. Prosessisuunnittelussa päädyttiin vaihtoehtoon, jossa tehtaan nykyinen tehdasvesijae korvataan jälkikäsitellyllä jätevesikirkasteella. Esitetty prosessimuutos vähentäisi jokeen laskettavan kirkasteen määrää 20 %. Haitta-ainetason muutoksia selvitettiin simuloimalla prosessisuunnitelman mukainen suolatase. Simuloinnin kohteena oli haitta-ainetason muutokset PK3:lla. Tuloksista pääteltiin, että PK3:lla tapahtuu normaalissa ajotilanteessa suurempia muutoksia suolatasoissa kuin prosessimuutoksen aiheuttama suolatason muutos. Arkkikokeilla selvitettiin kirkasteen ja tehdasveden vaikutuksia PK3:n massan vaaleuteen ja vaaleuden pysyvyyteen. Kirkasteen vaikutus massan vaaleuteen oli suurempi kuin tehdasvedellä, kun kirkastetta oli käsitelty tehdasmittakaavan flotaatiolla ja hiekkasuodatuksella. Pilot-mittakaavan hiekkasuodatuksella ja laboratoriomittakaavassa laskeutetulla kirkasteella oli pienempi vaikutus arkkien vaaleuteen kuin tehdasvedellä. Vaaleuden pysyvyydessä ei havaittu eroa kirkasteen ja tehdasveden välillä. Kirkasteella oli voimakas vaikutus arkkien keltaisuuteen. Tehdasvesi ei vaikuttanut arkkien keltaisuuteen. Mikäli prosessisuunnitelman mukainen kirkastevirtaus jatkokäsiteltäisiin hiekkasuodatuksella, arvioitiin päälaitteista kerroinmenetelmällä tehdasinvestoinniksi 5.20 milj. euroa. Vuosittaisiksi kemikaalikustannuksiksi arvioitiin 0.21 milj. euroa ja teoreettiseksi energiasäästöksi 0.87 milj. euroa.