The present study was undertaken to evaluate the filtration efficiency of the bath sponge Spongia ceylonensis (Spongiidae) and fire sponge Tedania klausi (Tedaniidae) collected from Penghu. In the feeding experiements, live and algal powder of Tetraselmis chui (8-16£gm), Chaetoceros muelleri (6-9£gm), Isochrysis galbana (3-7£gm) and Nannochloropsis oculata (2-5£gm) were used to determine the clearance rate of sponges. Sponges S. ceylonensis and T. klausi showed selective feeding under various algal species, concentrations and conditions (live algae or powders). After 90 minutes, the clearance rate of T. klausi fed on N. oculata powder was 71 ml h-1 gDW-1 at algal concentration of 107 cells ml-1, but S. ceylonensis didn¡¦t feed at the same concentration. At 106 cells ml-1 concentrations, the clearance rate of S. ceylonensis fed on live I. galbana was 538 ml h-1 gDW-1 which was higher than T. klausi, i.e. 11 ml h-1 gDW-1. At 105 cells ml-1 concentrations, the clearance rate of T. klausi fed on live T. chui was 431 ml h-1 gDW-1 which was higher than S. ceylonensis, i.e. 23 ml h-1 gDW-1. At 104 cells ml-1 concentrations, S. ceylonensis fed on live T. chui with clearance rate 532 ml h-1 gDW-1, and T. klausi was 315 ml h-1 gDW-1. The results showed differential clearance rates of sponges depend on sponge species, algal species, concentrations and conditions (live or powder). In gerneral, sponge clearance rate is higher when feeds on live algae than algal powders. Although the filtration efficiency of algal powders is low, the advantage of low cost and high accessibility still make algal powder highly competitive in sponge aquaculture industry.

No description available.

Submitted by RENATO ALVES CAVALCANTI (renatoa.cavalcanti@hotmail.com) on 2018-04-20T19:35:13Z No. of bitstreams: 1 DISSERTACAO final CD.doc: 1705472 bytes, checksum: b127c150094c6b7ffb1f73ed0519b39f (MD5) / Rejected by Alexandra Maria Donadon Lusser Segali null (alexmar@fcav.unesp.br), reason: Solicitamos que realize correções na submissão seguindo as orientações abaixo: O arquivo submetido ao repositório deve estar no formato pdf e não em formato word. Favor colocar em formato pdf desbloqueado segundo ite 13 do tutorial de auto arquivamento: Upload do arquivo 13. Para enviar o arquivo contendo sua dissertação ou tese é necessário que:  o arquivo esteja no formato Portable Document Format (PDF);  o arquivo não esteja protegido;  o trabalho (dissertação ou tese) esteja reunido em um único arquivo, inclusive os apêndices e anexos. https://portal.biblioteca.unesp.br/portal/arquivos/tutorial-para-o-autoarquivamento-de-dissertacoes-e-teses-2.0.pdf Agradecemos a compreensão on 2018-04-25T12:08:51Z (GMT) / Submitted by RENATO ALVES CAVALCANTI (renatoa.cavalcanti@hotmail.com) on 2018-04-25T14:47:43Z No. of bitstreams: 1 DISSERTACAO_RENATO_ALVES_CAVALCANTI.pdf: 1329114 bytes, checksum: 20d539d56c4e488c0120474cccea5252 (MD5) / Approved for entry into archive by Alexandra Maria Donadon Lusser Segali null (alexmar@fcav.unesp.br) on 2018-04-25T15:59:46Z (GMT) No. of bitstreams: 1 cavalcanti_ra_me_jabo.pdf: 1329114 bytes, checksum: 20d539d56c4e488c0120474cccea5252 (MD5) / Made available in DSpace on 2018-04-25T15:59:46Z (GMT). No. of bitstreams: 1 cavalcanti_ra_me_jabo.pdf: 1329114 bytes, checksum: 20d539d56c4e488c0120474cccea5252 (MD5) Previous issue date: 2018-02-23 / O objetivo deste trabalho foi desenvolver um protótipo de filtro para irrigação com crepina artesanal, submetido a regime de água residuária de suinocultura avaliando o desempenho hidráulico juntamente com a eficiência de filtragem, utilizando resíduos agrícolas (Maravalha, Casca de arroz, Crepina (sem elemento filtrante), Silagem de milho e Feno de Tifton (Cynodon spp.)) como elemento filtrante. A água residuária utilizada na experimentação foi coletada após a utilização do biodigestor. A hidrometria utilizando placa de orifício foi através do diferencial de pressão acusado na coluna de mercúrio tipo “U”. O processo de construção do protótipo de filtro foi a partir de meio metro tubo PVC azul, com diâmetro interno de 94,4 mm. Em uma das extremidades, foi inserido na parte interna, um cap PVC roscável de 1 polegada, com 115 furos de 1 milímetro. A esta peça, neste trabalho, foi atribuída o nome de Crepina. Pôde-se concluir nesta pesquisa, que o protótipo de filtro operou satisfatoriamente em termos estruturais e operacionais. O filtro operando sem elemento filtrante teve baixa perda de carga e eficiência de filtragem de sólidos totais de 34%. / The objective of this work was to develop a filter prototype for irrigation with artisanal crepine, to submit to the swine wastewater regime and to evaluate the hydraulic performance along with filtering efficiency, using agricultural residues (Shavings, Rice husk, Crepina, Corn silage and Tifton hay (Cynodon spp.)) as filter element. The wastewater used in the experiment was collected after using the biodigester. The hydrometry was through the pressure differential on the orifice plate accused in the mercury column type "U". The process of constructing the prototype filter was from half a meter blue PVC tube, with internal diameter of 94.4 mm. At one end, a 1-inch threadable PVC cap with 115 1-mm holes was inserted inside. This piece, in this work, was given the name Crepina. It could be concluded in this research that the prototype filter operated satisfactorily in structural and operational terms. And that artisanal crepine had a low head loss and a total solids filtration efficiency of 34%.

Activated carbons have been modif fed using reactive chemicals to produce adsorbents of enhanced hydrophobic character which will also be resistant to surface oxidation that results from exposure to humid air ("ageing"). The intention was that modification would not disrupt the carbon pore structure. The adsorptive properties of the modified carbons have been investigated using probe molecules Including nitrogen, water, hexane, and chloropicrin, and the ageing characteristics of the carbons, and the factors controlling the adsorption of a model hydrophobic vapour from high humidity air have been studied. Directly fluorinated carbons were unstable, probably due to weakly adsorbed fluorine. Treatment of these adsorbents with other chemicals indicated the potential of the technique for Introducing specific functional groups onto the carbon surface. Carbons modified using selective fluorinating reagents (hexafluoropropene and 1,1-difluoroethene) were more hydrophobic, and adsorbed hydrophobic vapours more efficiently from humid air in comparison to controls. These adsorbents aged, but at a reduced rate in comparison to control carbon. Carbons modified using chlorinating reagents (carbonyl chloride and chlorine) and treated with solvents to remove adsorbed reagent and/or reaction products were of improved hydrophobic character, and adsorbed hydrophobic vapours from humid air at least as efficiently as the control samples. More importantly, these carbons offered resistance to ageing effects. A study of the factors controlling the efficiency with which hydrophobic vapours; are adsorbed from humid air revealed that the surface chemistry of the carbon is important, but that under typical conditions of use, filter performance was limited by the rate at which water displaced by the organic vapour could be carried away by the airstream. The results illustrate that filters containing chemically modified activated carbon offer advantages when volatile hydrophobic contaminant vapours are present, and where ageing effects are an important mechanism by which filtration efficiency is degraded.

Granular gas bed filters have been used in industry for a considerable period and mathematical descriptions of dust capture have allowed rigorous design of static beds. Provision for bed movement and electrostatic augmentation, which allows much thinner continuous beds to be used, requires adaptation of design methods for these phenomena. Design methods that allow for this are developed for a cross-flow bed with vertical bed movement and a number of granule and dust types. Direct current charging is applied to the bed itself and to the particles before they enter the bed. In the case of electrostatic augmentation, it is shown that simple models of spherical particles describe the mechanism adequately. The advantages of pre-charging dust particles before they enter the bed are indicated by calculation and proved experimentally. Parameters to describe the enhancement of filtration efficiency by the collected dust are obtained experimentally. It is shown that the factors controlling re-entrainment vary with particle size. For the dust particles less than 1,5 micrometers in size, re-entrainment is linked closely to the electrostatic capture mechanism which is dominant in that size range. For particles approaching 10 micrometer, re-entrainment can be neglected as the impaction efficiency, which is dominant for particles of this size and larger, approaches unity. A complex situation exists between these particle sizes as the magnitude and predominance of capture mechanisms in this region are determined by a number of operational parameters. It did not prove possible to develop predictive equations for re-entrainment efficiency using the results of this study. A number of heuristics are however developed that allow rational design by the use of the empirical parameters found, and that will be valid for the range of parameters used in this work. / Thesis (PhD(Chemical Engineering))--University of Pretoria, 2006. / Chemical Engineering / unrestricted

<div>In this study, three ducts have been built in Herrick Labs, Purdue University, West Lafayette, representing the real HVAC systems. Different types of filters have been tested in each duct, including MERV8, MERV14 mechanical filters, and MERV13 electret filter. One of this study's main objectives is to compare in-situ filter performance with the MERV rating, which comes from laboratory testing. Eventually, we can explain the variations and have a better understanding of the in-situ filter performance. Another primary objective is to evaluate the aging process of tested filters. Typically, HVAC filters will not be replaced or maintained frequently, so they tend to stay in HVAC systems for an extended period. In this study, the evolution of filter aging performance is tested continuously for the experiment's entire duration, including temporal evolution of pressure drops, filtration efficiencies, and loaded particulate mass on the filter media.</div><div><br></div><div>This study will continue for 52 full weeks. This thesis is a part of the on-going study, including the data up to the first 18 weeks so far. As a result, the pressure drops are steadily increasing over time for most filters due to the natural filter loading process, except for the MERV13 electret filter, which shows no significant change at all. In terms of the filtration efficiencies, two efficiency categories are included: mass-based efficiencies (ePM x ) for sizeintegrated particulate mass (PM) and size-resolved efficiencies. It can be seen that there is no significant change in ePM x for MERV8 and MERV14 filters, MERV13 electret filter whereas shows a degradation in ePM x efficiencies. Size-resolve efficiencies provide additional filtration efficiencies as a function of particle sizes, therefore more comprehensive. It can be found that for MERV8 and MERV14 filters, the efficiencies are slowly increasing for particles above 300 nm, with some variations. MERV13 electret filter has an explicitly decreasing trend for efficiencies across all particle size ranges.</div><div><br></div><div>Besides the filter loading process, another component affecting the filter performance is the environmental factor, such as temperature, relative humidity (RH), and precipitation events, including rainfall and snowfall. As a result, it can be observed that when precipitation events, the pressure drops trend to decrease for that period. It is also evident that decreasing temperature tends to promote pressure drops.</div>

No description available.

L’imperméabilisation des surfaces et l’augmentation des débits de pointe sont liés au développement croissant des environnements urbains. Avec cette croissance urbaine, les processus de ruissellement sont largement affectés et représentent un secteur dans lequel des actions doivent être entreprises afin d’assurer à la fois le développement économique et la protection de l’environnement et des ressources en eau. Le ruissellement est fréquemment associé à des pollutions diffuses (Non Point Source) qui ne sont généralement pas prises en compte dans les dispositifs classiques de régulation hydraulique. L’objectif de cette recherche était d’évaluer les performance de dispositifs de filtration sur les micro particules polluantes diffuses issues des chaussées routières et des déversoirs d’orages des réseaux d’assainissement unitaires (Combined Sewer Overflows – CSOs). Le protocole expérimental implique de mesurer, dans un premier temps, la taille et les caractéristiques des particules polluantes diffuses et ensuite, de réaliser une procédure identique à la sortie des installations de filtration et de traitement. Les modifications dans la distribution de la taille des particules et de leurs caractéristiques sont alors analysées. Les quatre principaux dispositifs de filtration disponibles - Expanded Polypropylene (EPP), Expanded polystyrene (EPS), Perlite pour les particules flottantes et Zeolite pour les non flottantes – ont été implanté sur un équipement de test et les résultats comparés. Une modélisation 3D (CFD) a été réalisée afin d’optimiser la conception de la disposition de filtration. / The impermeable area and the peak discharge volume have been consistently increasing due to widening of city development and renewal. Thus, distortion of water cycle has been serious problem compared to the past. When it comes to NPS pollution, lack of information on the load and characteristics of pollutants led to the insufficient reduction measures. The purpose of this study is to investigate the effectiveness of filters to control micro particles from non-point sources, especially from road runoff and Combined Sewer Overflows (CSOs). The study first examined the particle size and characteristics of NPS pollutants, and then analyzed the head loss, treatment efficiency and changes in particle size distribution before and after the treatment using device type facilities. The four most commonly used filters - Expanded Polypropylene (EPP), Expanded polystyrene (EPS), and Perlite as floatability filtering materials, and Zeolite as non-floatability - were compared. The upward-type filtering equipment was manufactured for the lab experiment, and CFD modeling was conducted to identify optimized design parameters. The results showed that the ratio of micro particles(＜100 ㎛), to which the filtering process can be applied, was highest in samples from the road runoff, followed by one from the bridge, and from the parking lot. The results using road runoff displayed that EPP was most efficient with ratio of 89% to treat SS and COD.

La qualité microbienne de l’air intérieur représente un enjeu sanitaire important, notamment dans le secteur professionnel. Ces travaux de thèse ont permis d’étudier les conditions favorisant le développement des espèces microbiennes collectées sur des médias fibreux utilisés dans des CTA, ainsi que leur réentrainement an aval de la filtration, susceptible de dégrader la qualité de l’air. La première partie de l’étude s’est déroulée en laboratoire à partir de la filtration d’un consortium bactérien – fongique composé de Staphylococcus epidermidis et Penicillium oxalicum. L’influence de trois paramètres a été étudiée sur la croissance microbienne : le taux d’humidité relative (HR) de l’air, la nature du média fibreux, la présence/absence de flux d’air. Les résultats ont révélé notamment que quelles que soient les conditions,S. epidermidis n’arrive pas à croître. En revanche, lorsque l’HR de l’air approche 100%, P. oxalicum se développe sur les filtres et des spores sont relarguées en aval des filtres après une reprise de la filtration. Une seconde partie de l’étude a consisté à travailler avec un aérosol atmosphérique semi urbain. Deux unités de filtration d’air ont fonctionné pendant 5 mois en parallèle. La ventilation d’une des deux unités a été stoppée chaque week-end et redémarrée en début de semaine. Un suivi de la température, de l’humidité de l’air, de la perte de charge des filtres et de la concentration des particules totales dans l’air en amont de la filtration a été assuré tout au long de l’étude. Les concentrations en microorganismes cultivables ont été mesurées chaque semaine en amont et en aval de chaque filtre, notamment au redémarrage de la ventilation. En fonction des variations saisonnières de la concentration des microorganismes, les résultats ont montré en particulier des efficacités de filtration vis-à-vis des particules bactériennes faibles, voire négatives, dans l’unité de filtration fonctionnant en continu. / Microbial indoor air quality is an important issue in particular in the professional sector. This thesis aims to investigate the conditions leading to microbial development on to fibrous filters and to microbial release down stream of filters that could decrease air quality. The first part of the thesis was realized on laboratory and consisted in the filtration of a microbial consortium composed with Staphylococcus epidermidis (bacterium specie) and Penicillium oxalicum (fungi specie). The effects of three parameters on the microbial behavior were studied : the relative humidity (RH) of the air, the filter material, the airflow presence/absence. Whatever conditions, S. epidermidis did not grow up. However, P. oxalicum has demonstrated its ability to develop itself when RH was close to 100% and some P. oxalicumspores were released downstream of filter after growth, when ventilation was restarted. The second part of the thesis consisted in working with a semi-urban outdoor air. Two air handling unit (AHU) have operated during 5 months. The ventilation of one AHU was stopped each week-end and restarted each beginning of week. Temperature and RH of the air, filters pressure drop and total concentration of PM in air before filtration were monitored. Concentration of total cultivable microorganisms upstream and downstream of both filters was also measured each week, in particular at the restart of ventilation for one AHU. According to seasonal variations of microbial concentrations, results have revealed for instance that the filtration efficiency of cultivable bacteria was particularly weak, and sometimes negative, for the AHU operating continuously.

Made available in DSpace on 2016-06-02T19:56:59Z (GMT). No. of bitstreams: 1 6695.pdf: 5587762 bytes, checksum: 18422df241d7678995fda12c8a8bf70f (MD5) Previous issue date: 2015-01-23 / Universidade Federal de Sao Carlos / Human exposure to nanoparticles is increasingly becoming a concern, including in the workplace, due to urban and industrial development and the increasing use of motor vehicles. Filtration using fibrous filters is among the various options that can be used to provide efficient elimination of particles. It is known that there has been little research concerning the removal of nanoparticles using these filtration media. The aim of this study was to characterize, evaluate the efficiency and analyze the influence of filtration area on the efficiencies of the filter media HEPA (high efficiency particulate air), glass, micro-quartz, and polyester (300 g/m2) for the removal of nanoparticles. The filtration area was analyzed because is not possible in general to do the experimental testes in laboratory with large filtration area. The evaluation of the filter media depend on the structure of the filters (fiber diameter, thickness, and permeability), the operating conditions (superficial velocity and filtration area), and the characteristics of the filtered aerosols (density and size distribution). The characterization was used to evaluate the filter media and explain some results. Thickness, fiber diameter and permeability are examples of characterization parameters. The experimental setup was used in experimental tests of permeability and efficiency for the 5.3 and 40.7 cm2 filtration areas. A solution of 5 g/L sodium chloride (NaCl) was used to generate the nanoparticles in the filtration tests and a constant superficial velocity of 0.05 m/s. Particles were counted before and after passing through the filter media at the beginning of filtration using the electrical mobility technique. At the end of the filtration (one hour), the particles were again counted before and after the filters (in triplicate). The permeability constants of the HEPA, glass, and micro-quartz filters were the lower and they are influenced by the filtration area, while a much higher value was obtained for the polyester filter and showed no significant variation using different filtration area. Altogether, all the filter media were highly efficient in removing nanoparticles during approximately 2 hours of filtration, with the exception of the polyester filter, for which the efficiency decreased with increasing particle diameter. / Há uma grande preocupação com a exposição de pessoas às partículas nanométricas presentes no ar, até mesmo no ambiente de trabalho. Isto se deve ao desenvolvimento urbano, industrial e o crescente uso de veículos motorizados. Uma das soluções que vem sendo muito utilizadas ultimamente é o processo de filtração utilizando filtros fibrosos. Como há poucas pesquisas sobre o comportamento desses filtros na remoção de nanopartículas, o objetivo desse estudo foi caracterizar, avaliar a eficiência e verificar se o tamanho da área de filtração influencia no desempenho de meios filtrantes HEPA (High Efficiency Particulate Air Filter), de Vidro, de Micro Quartzo e de Poliéster na remoção de nanopartículas. A área de filtração foi avaliada uma vez que em testes laboratoriais nem sempre são possíveis grandes áreas de filtração para avaliação do desempenho de meios filtrantes. O desempenho de um meio filtrante depende da estrutura dos filtros (espessura, porosidade, diâmetro das fibras), das condições operacionais (velocidade de filtração e área de filtração) e das características do material particulado (densidade, tamanho da partícula e distribuição). A caracterização foi utilizada para avaliar os meios filtrantes e justificar possíveis resultados, entre ela está a espessura, o diâmetro das fibras e a permeabilidade. O sistema experimental foi utilizado tanto para a realização de experimentos de permeabilidade como para experimentos de eficiência com áreas de filtração iguais a 5,3cm2 e 40,7 cm2. Nos testes de eficiência foram utilizados uma solução de 5 g/L de cloreto de sódio para geração de partículas e velocidade constante de 5 cm/s. A contagem das partículas antes e após a passagem pelo meio filtrante era feita em triplicata no tempo zero e também depois de uma hora de filtração utilizando a técnica de mobilidade elétrica. Os meios filtrantes HEPA, de Vidro e de Quartzo apresentaram as menores constantes de permeabilidade e os valores foram ligeiramente influenciados pela área de filtração. Já o filtro de Poliéster foi o mais permeável e não apresentou variação significativa com a área de filtração. De uma forma geral, todos os meios filtrantes foram muito eficientes na remoção de nanopartículas durante duas horas de filtração aproximadamente, com exceção do filtro de Poliéster para o qual a eficiência decaiu com o aumento do tamanho das partículas.