57 resultados para pH-zone-refining counter-current chromatography

em Instituto Politécnico do Porto, Portugal


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The main objective of this study was to characterize the organic matter present in raw water and along the treatment process, as well as its seasonal variation. A natural organic matter fractionation approach has been applied to Lever water treatment plant located in Douro River, in Oporto (Portugal). The process used was based on the sorption of dissolved organic matter in different types of ion exchange resins, DAX-8, DAX-4 and IRA-958, allowing its separation into four fractions: very hydrophobic acids (VHA), slightly hydrophobic acids (SHA), charged hydrophilic (CHA) and hydrophilic neutral (NEU). The dissolved organic carbon (DOC) determination was used to quantify dissolved organic matter. Samples were collected monthly, during approximately one year, from raw water captured at the surface and under the bed of the river, and after each step of the treatment: pre-filtration in sand/anthracite filters, ozonation, coagulation/flocculation, counter current dissolved air flotation and filtration (CoCoDAFF) and chlorination. The NEU fraction showed a seasonal variation, with maximum values in autumn for the sampling points corresponding to raw water captured at the surface and under the bed of the river. It was usually the predominating fraction and did not show a significant decrease throughout the treatment. Nevertheless their low concentration, the same occurred for the CHA and VHA fractions. There was an overall decrease in the SHA fraction throughout the water treatment (especially after CoCoDAFF and ozonation) as well as in the DOC. The TSUVA254 values obtained for raw water generally varied between 2.0 and 4.0 L mgC-1 m-1 and between 0.75 and 1.78 L mgC-1 m-1 for treated water. It was observed a decrease of TSUVA values along the treatment, especially after ozonation. These results may contribute to a further optimization in the process of treating water for human consumption.

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A empresa Petibol, S.A. – Embalagens de plástico centra-se na produção de embalagens de plástico a partir da matéria-prima Poliestireno Expandido (EPS) e Polipropileno Expandido (EPP). A empresa possui uma preocupação ao nível da qualidade da água e do aproveitamento energético, tendo desta forma surgido a realização do estudo na unidade industrial, com o objectivo de anular e/ou diminuir as possíveis lacunas existentes na unidade industrial. Numa primeira etapa foi realizada uma caracterização global à qualidade da água e à empresa, actualizando-se os esquemas já existentes, contabilizando-se os custos actuais relativamente aos processos no circuito da água (arrefecimento, aquecimento e pressurização), e por fim, efectuou-se um levantamento in loco do circuito de água, relativamente à pressão, temperatura e caudal. Numa fase posterior, foram propostos equipamentos e processos, tendo em vista a colmatação dos problemas identificados, realizando-se um subsequente estudo relativamente aos custos inerentes a esses novos processos. A caracterização à água foi avaliada em diferentes pontos do circuito industrial, tendo-se determinado na Sala de Bombagem que o filtro de areia não possuía as dimensões mais apropriadas, existindo também um problema a nível mecânico associado ao processo de contra-lavagem. Tais factos podem ser a causa da ocorrência de um aumento do teor de sólidos após a passagem na camada filtrante. Relativamente ao amaciador, este deveria amaciar de forma completa a água para alimentação à caldeira, embora se tenha registado à saída do amaciador uma dureza de 21,3 mg/L, denunciando problemas na troca iónica. No que toca à água de alimentação à caldeira, verifica-se a existência de parâmetros que não se encontram de acordo com os critérios enunciados para uma óptima qualidade, sendo eles o pH (10,14), condutividade (363 μS/cm), teor de ferro (1,21 mg/L) e a dureza (16 mg/L). De salientar que somente o teor de cobre, que se encontra em quantidades vestigiais, apresenta-se de acordo com os valores impostos. No que respeita à água da caldeira, esta apresenta parâmetros incompatíveis com os recomendados, sendo eles a condutividade (7350 μS/cm), teor de sólidos dissolvidos (5248 mg/L) e alcalinidade total (780 mg/L). De referir que o valor de pH (11,8) não se encontra de acordo com a aplicação do tratamento “fosfato-pH coordenado”. Em relação aos parâmetros com valores que se encontram dentro dos limites, estes correspondem à dureza (0 mg/L), ao teor de fosfatos (45 mg/L) e teor de sílica (0 mg/L). A água do circuito de arrefecimento foi sujeita a uma análise microbiológica, que corroborou a presença de um biofilme. Um dos problemas enunciados pela empresa, prendia-se com a impossibilidade de descarga, no colector municipal, dos condensados dos compressores, visto apresentarem uma quantidade de óleo de cerca de 43,3 mg/L, equivalente a quatro vezes o valor limite de emissão, de acordo com a legislação municipal. Por fim, o efluente de descarga industrial apresenta um valor de pH (10,3) acima do intervalo permitido por lei (6,0 – 9,0), sendo que a corrente que mais contribui para este acréscimo de pH corresponde à corrente proveniente da água de purga, visto esta apresentar um valor de pH de 12,22. De maneira a contornar os parâmetros enunciados, é proposto a substituição do filtro de areia da Sala de Bombagem, assim como a inserção de um conjunto de medidas de remoção de ferro e desinfecção, sendo a conjugação de arejamento, coagulação, filtração e desinfecção, por parte do hipoclorito, a proposta apresentada. Aos condensados dos compressores é apresentado um sistema de separação, que possibilita a remoção do óleo da água, e uma consequente descarga da mesma. Actualmente, não existe qualquer filtro de areia no circuito de arrefecimento da água, sendo proposto assim esse equipamento, de forma a minorar o desenvolvimento da população microbiana, bem como a permitir uma maior eficiência na transferência de calor na torre de arrefecimento. Relativamente à descarga industrial, é recomendável a colocação de um sistema de regularização automática de pH. A inserção de uma válvula de três vias permite um aproveitamento energético e de água, a partir da confluência da água oriunda dos furos com a água do tanque de água fria, sendo posteriormente alimentada à central de vácuo. No estudo da recuperação energética, um outro equipamento avaliado correspondeu à serpentina, no entanto, verificou-se que a poupança no consumo de gás natural era de apenas 0,005%, o que não se mostrou uma proposta viável. O orçamento de todos os equipamentos é de 11.720,76 €, possibilitando não só um melhor funcionamento industrial, como um menor impacto a nível ambiental. Os custos futuros de funcionamento aumentam em 3,36%, tendo a pressurização um aumento do seu custo em 3,4% em relação ao custo actual, verificando-se um custo anual de 10.781,21€, em relação aos processos de arejamento, coagulação e desinfecção.

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Solvent extraction is considered as a multi-criteria optimization problem, since several chemical species with similar extraction kinetic properties are frequently present in the aqueous phase and the selective extraction is not practicable. This optimization, applied to mixer–settler units, considers the best parameters and operating conditions, as well as the best structure or process flow-sheet. Global process optimization is performed for a specific flow-sheet and a comparison of Pareto curves for different flow-sheets is made. The positive weight sum approach linked to the sequential quadratic programming method is used to obtain the Pareto set. In all investigated structures, recovery increases with hold-up, residence time and agitation speed, while the purity has an opposite behaviour. For the same treatment capacity, counter-current arrangements are shown to promote recovery without significant impairment in purity. Recycling the aqueous phase is shown to be irrelevant, but organic recycling with as many stages as economically feasible clearly improves the design criteria and reduces the most efficient organic flow-rate.

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Volatile organic compounds are a common source of groundwater contamination that can be easily removed by air stripping in columns with random packing and using a counter-current flow between the phases. This work proposes a new methodology for the column design for any particular type of packing and contaminant avoiding the necessity of a pre-defined diameter used in the classical approach. It also renders unnecessary the employment of the graphical Eckert generalized correlation for pressure drop estimates. The hydraulic features are previously chosen as a project criterion and only afterwards the mass transfer phenomena are incorporated, in opposition to conventional approach. The design procedure was translated into a convenient algorithm using C++ as programming language. A column was built in order to test the models used either in the design or in the simulation of the column performance. The experiments were fulfilled using a solution of chloroform in distilled water. Another model was built to simulate the operational performance of the column, both in steady state and in transient conditions. It consists in a system of two partial non linear differential equations (distributed parameters). Nevertheless, when flows are steady, the system became linear, although there is not an evident solution in analytical terms. In steady state the resulting system of ODE can be solved, allowing for the calculation of the concentration profile in both phases inside the column. In transient state the system of PDE was numerically solved by finite differences, after a previous linearization.

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Volatile organic compounds are a common source of groundwater contamination that can be easily removed by air stripping in columns with random packing and using a counter-current flow between the phases. This work proposes a new methodology for column design for any type of packing and contaminant which avoids the necessity of an arbitrary chosen diameter. It also avoids the employment of the usual graphical Eckert correlations for pressure drop. The hydraulic features are previously chosen as a project criterion. The design procedure was translated into a convenient algorithm in C++ language. A column was built in order to test the design, the theoretical steady-state and dynamic behaviour. The experiments were conducted using a solution of chloroform in distilled water. The results allowed for a correction in the theoretical global mass transfer coefficient previously estimated by the Onda correlations, which depend on several parameters that are not easy to control in experiments. For best describe the column behaviour in stationary and dynamic conditions, an original mathematical model was developed. It consists in a system of two partial non linear differential equations (distributed parameters). Nevertheless, when flows are steady, the system became linear, although there is not an evident solution in analytical terms. In steady state the resulting ODE can be solved by analytical methods, and in dynamic state the discretization of the PDE by finite differences allows for the overcoming of this difficulty. To estimate the contaminant concentrations in both phases in the column, a numerical algorithm was used. The high number of resulting algebraic equations and the impossibility of generating a recursive procedure did not allow the construction of a generalized programme. But an iterative procedure developed in an electronic worksheet allowed for the simulation. The solution is stable only for similar discretizations values. If different values for time/space discretization parameters are used, the solution easily becomes unstable. The system dynamic behaviour was simulated for the common liquid phase perturbations: step, impulse, rectangular pulse and sinusoidal. The final results do not configure strange or non-predictable behaviours.

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A detailed study of voltammetric behavior of ethiofencarb (ETF) is reported using glassy carbon electrode (GCE) and hanging mercury drop electrode (HMDE). With GCE, it is possible to verify that the oxidative mechanism is irreversible, independent of pH, and the maximum intensity current was observed at +1.20 V vs. AgCl/Ag at pH 1.9. A linear calibration line was obtained from 1.0x10-4 to 8.0x10-4 mol L-1 with SWV method. To complete the electrochemical knowledge of ETF pesticide, the reduction was also explored with HMDE. A well-defined peak was observed at –1.00V vs. AgCl/Ag in a large range of pH with higher signal at pH 7.0. Linearity was obtained in 4.2x10-6 and 9.4x10-6 mol L-1 ETF concentration range. An immediate alkaline hydrolysis of ETF was executed, producing a phenolic compound (2-ethylthiomethylphenol) (EMP), and the electrochemical activity of the product was examined. It was deduced that it is oxidized on GCE at +0.75V vs. AgCl/Ag with a maximum peak intensity current at pH 3.2, but the compound had no reduction activity on HMDE. Using the decrease of potential peak, a flow injection analysis (FIA) system was developed connected to an amperometric detector, enabling the determination of EMP over concentration range of 1.0x10-7 and 1.0x10-5 mol L-1 at a sampling rate of 60 h-1. The results provided by FIA methodology were performed by comparison with results from high-performance liquid chromatography (HPLC) technique and demonstrated good agreement with relative deviations lower than 4%. Recovery trials were performed and the obtained values were between 98 and 104%.

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The use of buffers to maintain the pH within a desired range is a very common practice in chemical, biochemical and biological studies. Among them, zwitterionic N-substituted aminosulfonic acids, usually known as Good’s buffers, although widely used, can complex metals and interact with biological systems. The present work reviews, discusses and updates the metal complexation characteristics of thirty one commercially available buffers. In addition, their impact on biological systems is also presented. The influences of these buffers on the results obtained in biological, biochemical and environmental studies, with special focus on their interaction with metal ions, are highlighted and critically reviewed. Using chemical speciation simulations, based on the current knowledge of the metal–buffer stability constants, a proposal of the most adequate buffer to employ for a given metal ion is presented.

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A literatura específica e o percurso da terapia ocupacional ilustram a continua preocupação e a percepção da importância da relação terapeuta/cliente para o sucesso da ocupação terapêutica e consequentes resultados positivos da terapia. Isto não significa que exista um grande aprofundamento desta temática e consensos quanto aos factores e competências que a influenciam e lhe estão inerentes. Apesar de haver algumas referências de como o terapeuta deve estar, não tem sido abordado como o terapeuta sente e vive a relação terapêutica. O objectivo principal deste estudo é contribuir para a importância da postura técnica e simultaneamente subjectiva de cada terapeuta ocupacional, no contexto terapêutico. Pretende-se perceber a forma como o terapeuta ocupacional vivência alguns aspectos que o acompanham no processo terapêutico que é manifesto nas suas atitudes e se reflectem na qualidade da intervenção terapêutica e complementarmente na sua vivência pessoal. Usou-se a metodologia qualitativa, a entrevista semi-estruturada e a análise de conteúdo, por valorizar a subjectividade, indo ao encontro do objectivo definido. A amostra integrou vinte terapeutas ocupacionais, com mais de dez anos de experiência profissional e cinco da actual área de especialização profissional - Crianças e Jovens; Medicina Física e Reabilitação, Saúde Mental Adultos e outra de diversos (Toxicodependência, Geriatria e Comunidade). Concluímos que a relação terapêutica em terapia ocupacional é referida como sendo o primeiro passo no investimento terapêutico, para a maioria não é considerada um procedimento técnico, mas produto do bom senso, “dom” da pessoa / terapeuta e vivenciam as emoções e sentimentos do contexto terapêutico, solitariamente e ou com a família, alguns com colegas e poucos numa equipa organizada.

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Involving groups in important management processes such as decision making has several advantages. By discussing and combining ideas, counter ideas, critical opinions, identified constraints, and alternatives, a group of individuals can test potentially better solutions, sometimes in the form of new products, services, and plans. In the past few decades, operations research, AI, and computer science have had tremendous success creating software systems that can achieve optimal solutions, even for complex problems. The only drawback is that people don’t always agree with these solutions. Sometimes this dissatisfaction is due to an incorrect parameterization of the problem. Nevertheless, the reasons people don’t like a solution might not be quantifiable, because those reasons are often based on aspects such as emotion, mood, and personality. At the same time, monolithic individual decisionsupport systems centered on optimizing solutions are being replaced by collaborative systems and group decision-support systems (GDSSs) that focus more on establishing connections between people in organizations. These systems follow a kind of social paradigm. Combining both optimization- and socialcentered approaches is a topic of current research. However, even if such a hybrid approach can be developed, it will still miss an essential point: the emotional nature of group participants in decision-making tasks. We’ve developed a context-aware emotion based model to design intelligent agents for group decision-making processes. To evaluate this model, we’ve incorporated it in an agent-based simulator called ABS4GD (Agent-Based Simulation for Group Decision), which we developed. This multiagent simulator considers emotion- and argument based factors while supporting group decision-making processes. Experiments show that agents endowed with emotional awareness achieve agreements more quickly than those without such awareness. Hence, participant agents that integrate emotional factors in their judgments can be more successful because, in exchanging arguments with other agents, they consider the emotional nature of group decision making.

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A multiresidue gas chromatographic method for the determination of six fungicides (captan, chlorthalonil, folpet, iprodione, procymidone and vinclozolin) and one acaricide (dicofol) in still and fortified wines was developed. Solid-phase microextraction (SPME) was chosen for the extraction of the compounds from the studied matrices and tandem mass spectrometry (MS/MS) detection was used. The extraction consists in a solvent free and automated procedure and the detection is highly sensitive and selective. Good linearity was obtained with correlation coefficients of regression (R2) > 0.99 for all the compounds. Satisfactory results of repeatability and intermediate precision were obtained for most of the analytes (RSD < 20%). Recoveries from spiked wine ranged from 80.1% to 112.0%. Limits of quantification (LOQs) were considerably below the proposedmaximumresidue limits (MRLs) for these compounds in grapes and below the suggested limits for wine (MRLs/10), with the exception of captan.

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We have developed a new method for single-drop microextraction (SDME) for the preconcentration of organochlorine pesticides (OCP) from complex matrices. It is based on the use of a silicone ring at the tip of the syringe. A 5 μL drop of n-hexane is applied to an aqueous extract containing the OCP and found to be adequate to preconcentrate the OCPs prior to analysis by GC in combination with tandem mass spectrometry. Fourteen OCP were determined using this technique in combination with programmable temperature vaporization. It is shown to have many advantages over traditional split/splitless injection. The effects of kind of organic solvent, exposure time, agitation and organic drop volume were optimized. Relative recoveries range from 59 to 117 %, with repeatabilities of <15 % (coefficient of variation) were achieved. The limits of detection range from 0.002 to 0.150 μg kg−1. The method was applied to the preconcentration of OCPs in fresh strawberry, strawberry jam, and soil.

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Total petroleum hydrocarbons (TPH) are important environmental contaminants which are toxic to human and environmental receptors. Several analytical methods have been used to quantify TPH levels in contaminated soils, specifically through infrared spectrometry (IR) and gas chromatography (GC). Despite being two of the most used techniques, some issues remain that have been inadequately studied: a) applicability of both techniques to soils contaminated with two distinct types of fuel (petrol and diesel), b) influence of the soil natural organic matter content on the results achieved by various analytical methods, and c) evaluation of the performance of both techniques in analyses of soils with different levels of contamination (presumably non-contaminated and potentially contaminated). The main objectives of this work were to answer these questions and to provide more complete information about the potentials and limitations of GC and IR techniques. The results led us to the following conclusions: a) IR analysis of soils contaminated with petrol is not suitable due to volatilisation losses, b) there is a significant influence of organic matter in IR analysis, and c) both techniques demonstrated the capacity to accurately quantify TPH in soils, irrespective of their contamination levels.

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Ibuprofen is one of the most used active pharmaceutical ingredients worldwide. A new method for the analysis of ibuprofen and its metabolites, hydroxyibuprofen and carboxyibuprofen, in soils is presented. The extraction of these compounds from the soil matrices was performed by using a modified quick, easy, cheap, effective, rugged, and safe (QuEChERS) method. The method involves a single extraction of the investigated compounds with purified water (acidified at pH 2.5 with hydrochloric acid), and a slow and continuous addition of the QuEChERS content, followed by the addition of acidified acetonitrile (1% acetic acid), prior to the determination by liquid chromatography coupled with fluorescence detection (LC–FLD). Validation studies were carried out using soil samples with a range of organic carbon contents. Recoveries of the fortified samples ranged from 79.5% to 101%. Relative standard deviations for all matrix–compound combinations did not exceed 3%. The method quantification limits were ≤22.4 μg kg−1 in all cases. The developed method was applied to the analysis of sixteen real samples.

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Scientific evidence has shown an association between organochlorine compounds (OCC) exposure and human health hazards. Concerning this, OCC detection in human adipose samples has to be considered a public health priority. This study evaluated the efficacy of various solid-phase extraction (SPE) and cleanup methods for OCC determination in human adipose tissue. Octadecylsilyl endcapped (C18-E), benzenesulfonic acid modified silica cation exchanger (SA), poly (styrene-divinylbenzene (EN) and EN/RP18 SPE sorbents were evaluated. The relative sample cleanup provided by these SPE columns was evaluated using gas chromatography with electron capture detection (GC–ECD). The C18-E columns with strong homogenization were found to provide the most effective cleanup, removing the greatest amount of interfering substance, and simultaneously ensuring good analyte recoveries higher than 70%. Recoveries>70% with standard deviations (SD)<15% were obtained for all compounds under the selected conditions. Method detection limits were in the 0.003–0.009 mg/kg range. The positive samples were confirmed by gas chromatography coupled with tandem mass spectrometry (GC-MS/MS). The highest percentage found of the OCC in real samples corresponded to HCB, o,p′-DDT and methoxychlor, which were detected in 80 and 95% of samples analyzed respectively. Copyright © 2012 John Wiley & Sons, Ltd.

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Multiclass analysis method was optimized in order to analyze pesticides traces by gas chromatography with ion-trap and tandem mass spectrometry (GC-MS/MS). The influence of some analytical parameters on pesticide signal response was explored. Five ion trap mass spectrometry (IT-MS) operating parameters, including isolation time (IT), excitation voltage (EV), excitation time (ET),maximum excitation energy or “q” value (q), and isolationmass window (IMW) were numerically tested in order to maximize the instrument analytical signal response. For this, multiple linear regression was used in data analysis to evaluate the influence of the five parameters on the analytical response in the ion trap mass spectrometer and to predict its response. The assessment of the five parameters based on the regression equations substantially increased the sensitivity of IT-MS/MS in the MS/MS mode. The results obtained show that for most of the pesticides, these parameters have a strong influence on both signal response and detection limit.Using the optimized method, a multiclass pesticide analysis was performed for 46 pesticides in a strawberry matrix. Levels higher than the limit established for strawberries by the European Union were found in some samples.