Application of heterogeneous vacancy solution theory to characterization of microporous solids

The vacancy solution theory of adsorption is re-formulated here through the mass-action law, and placed in a convenient framework permitting the development of thermodynamic ally consistent isotherms. It is shown that both the multisite Langmuir model and the classical vacancy solution theory expression are special cases of the more general approach when the Flory-Huggins activity coefficient model is used, with the former being the thermodynamically consistent result. The improved vacancy solution theory approach is further extended here to heterogeneous adsorbents by considering the pore-width dependent potential along with a pore size distribution. However, application of the model to numerous hydrocarbons as well as other adsorptives on microporous activated carbons shows that the multisite model has difficulty in the presence of a pore size distribution, because pores of different sizes can have different numbers of adsorbed layers and therefore different site occupancies. On the other hand, use of the classical vacancy solution theory expression for the local isotherm leads to good simultaneous fit of the data, while yielding a site diameter of about 0.257 nm, consistent with that expected for the potential well in aromatic rings on carbon pore surfaces. It is argued that the classical approach is successful because the Flory-Huggins term effectively represents adsorbate interactions in disguise. When used together with the ideal adsorbed solution theory the heterogeneous vacancy solution theory successfully predicts binary adsorption equilibria, and is found to perform better than the multisite Langmuir as well as the heterogeneous Langmuir model. (C) 2001 Elsevier Science Ltd. All rights reserved.

Porous solids from layered clays by combined pillaring and templating approaches

The pore structure formation in bentonite, pillared with a mixed sol of silicon and titanium hydroxides and treated subsequently with quaternary ammonium surfactants, is investigated. The surfactant micelles act as a template, similar to their role in MCM41 synthesis. Because both the surfactant micelles and the sol particles are positively charged, it is greatly favorable for them to form meso-phase assembles in the galleries between the clay layers that bear negative charges. Besides, the sol particles do not bond the clay layers strongly as other kinds of pillar precursors do, so that the treatment with surfactants can result in radical structure changes in sol-pillared clays. This allows us to tailor the pore structure of these porous clays by choice of surfactant. The surfactant treatment also results in profound increases in porosity and improvement in thermal stability. Therefore, the product porous clays have great potential to be Used to deal with large molecules or at high operating temperatures. We also found that titanium in these samples is highly dispersed in the silica matrix rather than existing in the form of small particles of pure titania. Such highly dispersed Ti active centers may offer excellent activities for catalytic oxidation reactions such as alkanes into alcohols and ketones.

Effect of soil composition and dissolved organic matter on pesticide sorption

The effect of the solid and dissolved organic matter fractions, mineral composition and ionic strength of the soil solution on the sorption behaviour of pesticides were studied. A number of soils, chosen so as to have different clay mineral and organic carbon content, were used to study the sorption of the pesticides atrazine (6-chloro-N-2-ethyl-N-4-isopropyl-1,3,5-triazine-2,4-diamine), 2,4-D ((2,4-dichlorophenoxy) acetic acid), isoproturon (3-(4-isopropylphenyl)1,1-dimethylurea) and paraquat (1,1'-dimethyl-4,4'-bipyridinium) in the presence of low and high levels of dissolved organic carbon and different background electrolytes. The sorption behaviour of atrazine, isoproturon and paraquat was dominated by the solid state soil components and the presence of dissolved organic matter had little effect. The sorption of 2,4-D was slightly affected by the soluble organic matter in the soil. However, this effect may be due to competition for adsorption sites between the pesticide and the soluble organic matter rather than due to a positive interaction between the pesticide and the soluble fraction of soil organic matter. It is concluded that the major factor governing the sorption of these pesticides is the solid state organic fraction with the clay mineral content also making a significant contribution. The dissolved organic carbon fraction of the total organic carbon in the soil and the ionic strength of the soil solution appear to have little or no effect on the sorption/transport characteristics of these pesticides over the range of concentrations studied. (C) 2002 Elsevier Science B.V. All rights reserved.

A mathematical model of concentrate solids content for the wet drum magnetic separator

Low concentrate density from wet drum magnetic separators in dense medium circuits can cause operating difficulties due to inability to obtain the required circulating medium density and, indirectly, high medium solids losses. The literature is almost silent on the processes controlling concentrate density. However, the common name for the region through which concentrate is discharged-the squeeze pan gap-implies that some extrusion process is thought to be at work. There is no model of magnetics recovery in a wet drum magnetic separator, which includes as inputs all significant machine and operating variables. A series of trials, in both factorial experiments and in single variable experiments, was done using a purpose built rig which featured a small industrial scale (700 mm lip length, 900 turn diameter) wet drum magnetic separator. A substantial data set of 191 trials was generated in this work. The results of the factorial experiments were used to identify the variables having a significant effect on magnetics recovery. It is proposed, based both on the experimental observations of the present work and on observations reported in the literature, that the process controlling magnetic separator concentrate density is one of drainage. Such a process should be able to be defined by an initial moisture, a drainage rate and a drainage time, the latter being defined by the volumetric flowrate and the volume within the drainage zone. The magnetics can be characterised by an experimentally derived ultimate drainage moisture. A model based on these concepts and containing adjustable parameters was developed. This model was then fitted to a randomly chosen 80% of the data, and validated by application to the remaining 20%. The model is shown to be a good fit to data over concentrate solids content values from 40% solids to 80% solids and for both magnetite and ferrosilicon feeds. (C) 2003 Elsevier Science B.V. All rights reserved.

Otimização da Amostragem e Estudo de Viabilidade da Monitorização de Sondas na ETAR de Rabada

Mestrado em Engenharia Química - Tecnologias de Protecção Ambiental

Avaliação do efeito da microfauna do tanque de arejamento no efluente final

O presente trabalho, efetuado na Estação de Tratamento de Águas Residuais do Freixo (ETAR do Freixo), decorreu durante um período de nove meses, (entre Dezembro de 2012 e Agosto de 2013), e teve como principais objetivos: - a observação microscópica e respetiva identificação dos organismos presentes nas lamas ativadas dos reatores biológicos da ETAR (incidindo nos protozoários, metazoários e bactérias filamentosas); - estabelecer a relação entre os organismos identificados/quantidade respetiva e a sedimentabilidade das lamas ativadas e sua influência no processo de depuração; - avaliar a variação das espécies identificadas com as alterações processuais. Para o efeito, a metodologia utilizada foi: - a colheita diária de amostras em vários pontos da ETAR; - a determinação dos parâmetros operacionais e caracterização das amostras recolhidas, tendo sido efetuadas 6039 análises físico-químicas, incluindo ao afluente à ETAR, ao afluente e ao conteúdo dos dois reatores biológicos, à corrente de recirculação de lamas e ao efluente; - a visualização diária microscópica ótica sem contraste de fase dos microrganismos presentes nos reatores biológicos; - a visualização microscópica ótica com contraste de fase da microfauna presente nos reatores biológicos, sendo efetuadas 16 identificações e quantificações dos protozoários presentes nas lamas ativadas dos dois reatores e 10 identificações e quantificações das bactérias filamentosas presentes nos dois reatores biológicos. O início do estudo ocorreu num período em que se começou a verificar um aumento excessivo de espumas nos decantadores secundários, resultando numa fraca sedimentabilidade das lamas e numa menor qualidade do efluente final. Na tentativa de reduzir a excessiva ascensão do manto de lamas que se verificou, foram efectuadas alterações operacionais, consistindo: - na alteração da razão de recirculação da decantação secundária para os reatores biológicos; - na introdução de um composto altamente concentrado em matéria orgânica na corrente de recirculação de lamas; - na alteração da extração de lamas biológicas. Verificou-se que as alterações processuais efetuadas foram muito eficazes na diminuição do manto de lamas da decantação secundária, bem como muito eficazes na qualidade do efluente final. Durante os meses de Fevereiro a Agosto fez-se o acompanhamento diário de todas as condições de operação de modo a manter e validar o procedimento de operação, o qual se considerou muito eficaz em termos de obtenção de uma água tratada de excelente qualidade. Durante o estudo efetuado, verificou-se que a população microbiológica existente nos dois reatores biológicos se manteve praticamente inalterada durante todo o período, sendo os móveis de fundo e os sésseis os grupos dominantes. Esta dominância traduziu-se na elevada qualidade do efluente final que se observou a partir do mês de Fevereiro, tendo dificultado o estudo de novas condições de operação, mas facilitando a validação do procedimento adotado. No que se refere às bactérias filamentosas, verificou-se que são diversas as espécies presentes nos reatores biológicos e que existem em grande abundância, sendo que o Tipo 0092 é claramente dominante. O excessivo crescimento deste tipo de bactérias mostrou ser o maior problema a nível microbiológico no processo de tratamento da instalação, tornando-se crítico no período de inverno em que a temperatura e os picos de pluviosidade se mostraram condições favoráveis ao seu desenvolvimento. Para além da temperatura outros fatores mostraram-se responsáveis pelo seu crescimento tais como a razão Alimento/Microrganismo (A/M), a idade das lamas, a carga mássica afluente e o teor de oxigénio dissolvido nos reatores biológicos. Pode-se concluir que apesar de não se trabalhar com os valores teóricos dos parâmetros microbiológicos e operacionais considerados ideais, a ETAR do Freixo, possui um tratamento bastante eficaz na remoção da carga orgânica, na remoção de nutrientes e na remoção de sólidos suspensos totais, apesar da não existência de uma etapa de afinação final como a filtração.

Avaliação e Otimização do Consumo de Água no Processo e do Sistema de Tratamento de Efluentes

O elevado consumo de água associado à escassez deste recurso contribuiu para que alternativas de reutilização/reciclagem de água fossem estudadas que permitam diminuir o seu consumo e minimizar a dependência das indústrias. Monitorizar e avaliar os consumos de água, a nível industrial, é imprescindível para assegurar uma gestão sustentável dos recursos hídricos, sendo este o objetivo da presente dissertação. As alternativas encontradas na unidade industrial em estudo foram a substituição do equipamento sanitário e o aproveitamento do efluente tratado para operações de lavagem e/ou arrefecimento por contacto direto. A maioria do equipamento sanitário não é eficiente, tendo-se proposto a substituição desse sistema por um de menor consumo que permitirá uma poupança de 30 % no consumo de água, que corresponderá a 12 149,37 €/ano, sendo o retorno do investimento estimado em 3 meses. O efluente industrial na entrada da ETAR e nas diferentes etapas - tratamento primário de coagulação/floculação; tratamento secundário ou biológico em SBR; tratamento terciário de coagulação/floculação - foi caracterizado através da medição da temperatura, pH, oxigénio dissolvido e pela determinação da cor, turvação, sólidos suspensos totais (SST), azoto total, carência química de oxigénio (CQO), Carência Bioquímica de Oxigénio ao fim de 5 dias (CBO5) e razão CBO5/CQO. Esta caracterização permitiu avaliar o efluente industrial bruto que se caracteriza por um pH alcalino (8,3 ± 1,7); condutividade baixa (451 ± 200,2 μS/cm); elevada turvação (11 255 ± 8812,8 FTU); cor aparente (63 670 ± 42293,4 PtCo) e cor verdadeira (33 621 ± 19547,9 PtCo) elevadas; teores elevados de CQO (24 753 ± 11806,7 mg/L O2) SST (5 164 ± 3845,5 mg/L) e azoto total (718 mg/L) e um índice de biodegradabilidade baixo (razão CBO5/CQO de 1,4). Este estudo permitiu verificar que a eficiência global do tratamento do efluente foi 82 % na remoção da turvação, 83 % na remoção da cor aparente, 96 % na remoção da cor verdadeira, 85 % na remoção da CQO e 30 % na remoção dos SST. Quanto às eficiências de remoção associadas ao tratamento primário no que diz respeito à turvação, cor aparente, CQO e SST, apresentam valores inferiores aos referidos na literatura para o mesmo tipo de tratamento em efluentes similares. As eficiências de remoção obtidas no tratamento secundário são inferiores às do tratamento primário: turvação, cor aparente, CQO e SST, pelo que procurou-se otimizar a primeira etapa do processo de tratamento Neste estudo de otimização estudou-se a influência de cinco coagulantes – Sulfato de Alumínio, PAX XL – 10, PAX 18, cloreto de ferro e a conjugação de PAX 18 com sulfato de ferro - e seis floculantes – Superfloc A 150, Superfloc A 130, PA 1020, Ambifloc 560, Ambifloc C58 e Rifloc 54 - no tratamento físico-químico do efluente. O PAX 18 e o Ambifloc 560 UUJ foram os que apresentaram as mais elevadas eficiências de remoção (99,85 % na cor, 99,87 % na turvação, 90,12 % na CQO e 99,87 % nos SST). O custo associado a este tratamento é de 1,03 €/m3. Pela comparação com os critérios de qualidade no guia técnico ERSAR, apenas o parâmetro da CQO excede o valor, contudo o valor obtido permite diminuir os custos associados a um tratamento posterior para remoção da CQO remanescente no efluente residual tratado.

Dissolved organic nitrogen behaviour during denitrification with suspended and attached biomass

Dissertação para obtenção do Grau de Mestre em Engenharia do Ambiente, perfil Engenharia Sanitária

Spatial-temporal variation of dissolved inorganic material in the Amazon basin

The Amazon River basin is important in the contribution of dissolved material to oceans (4% worldwide). The aim of this work was to study the spatial and the temporal variability of dissolved inorganic materials in the main rivers of the Amazon basin. Data from 2003 to 2011 from six gauging stations of the ORE-HYBAM localized in Solimões, Purus, Madeira and Amazon rivers were used for this study. The concentrations of Ca2+, Na+, K+, Mg2+, Cl-, SO4 -2, HCO3 - and SiO2 were analyzed. At the stations of Solimões and Amazon rivers, the concentrations of Ca2+, Mg2+, HCO3 - and SO4 -2 had heterogeneous distribution over the years and did not show seasonality. At the stations of Madeira river, the concentration of these ions had seasonality inversely proportional to water discharge (dilution-concentration effect). Similar behavior was observed for the concentrations of Cl- and Na+ at the stations of the Solimões, Amazon and Madeira rivers, indicating almost constant release of Cl- and Na+ fluxes during the hydrological cycle. K+ and SiO2 showed almost constant concentrations throughout the years and all the stations, indicating that their flows depend on the river discharge variation. Therefore, the temporal variability of the dissolved inorganic material fluxes in the Solimões and Amazon rivers depends on the hydro-climatic factor and on the heterogeneity of the sources. In the Madeira and Purus rivers there is less influence of these factors, indicating that dissolved load fluxes are mainly associated to silicates weathering. As the Solimões basin contributes approximately 84% of the total flux of dissolved materials in the basin and is mainly under the influence of a hydro-climatic factor, we conclude that the temporal variability of this factor controls the temporal variability of the dissolved material fluxes of the Amazon basin.

Anatomy of contaminated aquifers of an industrial site: insights from the stable isotope compositions of waters and dissolved inorganic carbon

The hydrogen and oxygen isotopes of water and the carbon isotope composition of dissolved inorganic carbon (DIC) from different aquifers at an industrial site, highly contaminated by organic pollutants representing residues of the former gas production, have been used as natural tracers to characterize the hydrologic system. On the basis of their stable isotope compositions as well as the seasonal variations, different groups of waters (precipitation, surface waters, groundwaters and mineral waters) as well as seasonably variable processes of mixing between these waters can clearly be distinguished. In addition, reservoir effects and infiltration rates can be estimated. In the northern part of the site an influence of uprising mineral waters within the Quaternary aquifers, presumably along a fault zone, can be recognized. Marginal infiltration from the Neckar River in the cast and surface water infiltration adjacent to a steep hill on the western edge of the site with an infiltration rate of about one month can also be resolved through the seasonal variation. Quaternary aquifers closer to the centre of the site show no seasonal variations, except for one borehole close to a former mill channel and another borehole adjacent to a rain water channel. Distinct carbon isotope compositions and concentrations of DIC for these different groups of waters reflect variable influence of different components of the natural carbon cycle: dissolution of marine carbonates in the mineral waters, biogenic, soil-derived CO2 in ground- and surface waters, as well as additional influence of atmospheric CO2 for the surface waters. Many Quaternary aquifer waters have, however, distinctly lower delta(13)C(DIC) values and higher DIC concentrations compared to those expected for natural waters. Given the location of contaminated groundwaters at this site but also in the industrially well-developed valley outside of this site, the most likely source for the low C-13(DIC) values is a biodegradation of anthropogenic organic substances, in particular the tar oils at the site.

Non-invasive detection of cocaine dissolved in wine bottles by (1) H magnetic resonance spectroscopy.

Recently, a number of cases of smuggling dissolved cocaine in wine bottles have been reported. The aim of the present study was to determine whether cocaine dissolved in wine can be detected by proton magnetic resonance spectroscopy ((1) H MRS) on a standard clinical MR scanner, in intact (i.e. unopened) wine bottles. (1) H MRS experiments were performed with a 3 Tesla clinical scanner on wine phantoms with or without cocaine contamination. The aromatic protons of cocaine displayed resonance peaks in the 7-8 ppm region of the spectrum, where no overlapping resonances of wine were present. Additional cocaine resonances were detected in the 2-3 ppm region of the spectrum, between the resonances of ethanol and other wine constituents. Detection of cocaine in wine (at 5 mM, i.e. ∼1.5 g/L) was feasible in a scan time of 1 min. We conclude that dissolved cocaine can be detected in intact wine bottles, on a standard clinical MR scanner. Thus, (1) H MRS is the technique of choice to examine this type of suspicious cargo, since it allows for a non-destructive and rapid content characterization. Copyright © 2010 John Wiley & Sons, Ltd.

Quantitative comparison of simulations of seismic wave propagation in heterogeneous poro-elastic media involving fluid-solid interfaces and in equivalent visco-elastic solids

There is increasing evidence to suggest that the presence of mesoscopic heterogeneities constitutes the predominant attenuation mechanism at seismic frequencies. As a consequence, centimeter-scale perturbations of the subsurface physical properties should be taken into account for seismic modeling whenever detailed and accurate responses of the target structures are desired. This is, however, computationally prohibitive since extremely small grid spacings would be necessary. A convenient way to circumvent this problem is to use an upscaling procedure to replace the heterogeneous porous media by equivalent visco-elastic solids. In this work, we solve Biot's equations of motion to perform numerical simulations of seismic wave propagation through porous media containing mesoscopic heterogeneities. We then use an upscaling procedure to replace the heterogeneous poro-elastic regions by homogeneous equivalent visco-elastic solids and repeat the simulations using visco-elastic equations of motion. We find that, despite the equivalent attenuation behavior of the heterogeneous poro-elastic medium and the equivalent visco-elastic solid, the seismograms may differ due to diverging boundary conditions at fluid-solid interfaces, where there exist additional options for the poro-elastic case. In particular, we observe that the seismograms agree for closed-pore boundary conditions, but differ significantly for open-pore boundary conditions. This is an interesting result, which has potentially important implications for wave-equation-based algorithms in exploration geophysics involving fluid-solid interfaces, such as, for example, wave field decomposition.

Evaluación ambiental en la zona marino costera de Lambayeque – Perú, 2010.

Se realizaron 2 evaluaciones, en agosto y noviembre-diciembre 2010, entre la desembocadura del Dren 1000 (Bodegones) y la del río Zaña. En el intermareal se registró la mayor temperatura superficial del mar, se registró anomalías de hasta +8,1°C (desembocadura del Dren 1000). En agosto en el submareal, la temperatura promedio fue 16,3 °C; en noviembre-diciembre fue 15,9 °C. Similar tendencia en superficie y fondo se observó en el oxígeno disuelto. Mayor cantidad de sólidos suspendidos totales (SST) se registró alrededor de la desembocadura del Dren 4000 (137,93 mg/L), sobrepasando los límites permisibles para aguas de CEMC y AMC. Aceites y grasas fluctuaron entre 0 y 0,3 mg/L encontrándose dentro de los límites permisibles de CEMC y AMC. En el submareal, los Coliformes Totales (CT) y coliformes Termotolerantes (CTT) cumplieron con la Ley General de Aguas para la clase V y VI; en el intermareal la demanda bioquímica de oxigeno (DBO5) en la desembocadura del Dren 3100, sobrepasó los límites permisibles de calidad de agua. En agosto se registraron 39 especies en el bentos, en noviembre y diciembre fueron 27 especies. Los índices de diversidad de Shannon Wiener y riqueza de especies del macrobentos submareal, se incrementaron de norte a sur, debido al predominio del sustrato fango-arenoso. Los puntos de alteración ambiental fueron las desembocaduras de los drenes 1000, 3100 y 4000, que reciben aguas servidas y desechos orgánicos e industriales de los centros poblados de Lambayeque, Pimentel y Santa Rosa, respectivamente.