10 resultados para ADSORPTIVE STRIPPING VOLTAMMETRY


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Journal of Electroanalytical Chemistry 541 (2003) 153-162

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Applied Physics Letters, 89

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Dissertação para obtenção do Grau de Mestre em Biotecnologia

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Dissertação para obtenção do Grau de Mestre em Biotecnologia

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J Biol Inorg Chem (2010) 15:967–976 DOI 10.1007/s00775-010-0658-6

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J Biol Inorg Chem (2007) 12:691–698 DOI 10.1007/s00775-007-0219-9

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Dissertação para obtenção do Grau de Doutor em Química

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Understanding how the brain works will require tools capable of measuring neuron elec-trical activity at a network scale. However, considerable progress is still necessary to reliably increase the number of neurons that are recorded and identified simultaneously with existing mi-croelectrode arrays. This project aims to evaluate how different materials can modify the effi-ciency of signal transfer from the neural tissue to the electrode. Therefore, various coating materials (gold, PEDOT, tungsten oxide and carbon nano-tubes) are characterized in terms of their underlying electrochemical processes and recording ef-ficacy. Iridium electrodes (177-706 μm2) are coated using galvanostatic deposition under different charge densities. By performing electrochemical impedance spectroscopy in phosphate buffered saline it is determined that the impedance modulus at 1 kHz depends on the coating material and decreased up to a maximum of two orders of magnitude for PEDOT (from 1 MΩ to 25 kΩ). The electrodes are furthermore characterized by cyclic voltammetry showing that charge storage capacity is im-proved by one order of magnitude reaching a maximum of 84.1 mC/cm2 for the PEDOT: gold nanoparticles composite (38 times the capacity of the pristine). Neural recording of spontaneous activity within the cortex was performed in anesthetized rodents to evaluate electrode coating performance.

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O trabalho realizado foi desenvolvido no âmbito de um estágio curricular de seis meses realizado na Refinaria de Sines da Galp Energia. O principal objetivo foi a otimização da maior coluna de destilação de vácuo existente, uma vez que com o início do funcionamento de novas unidades, como é o caso do Hydrocraker, a produção de gasóleo de vácuo na Refinaria não é suficiente para assegurar a carga das unidades sendo necessário importar, diminuindo assim as margens das unidades. Foi implementada a simulação da coluna de destilação de vácuo II em ASPEN PLUS® para o caso de design, usando as condições de operação que o licenciador usou nas suas simulações para o re-vamping da unidade. Posteriormente foi efetuada a implementação para o caso de Test Run, em que são verificadas as produções projetadas para a coluna, e foram implementados na coluna 4 casos de operação real, onde foram recolhidos os dados de operação e comparadas as características dos produtos simulados com os resultados obtidos nos ensaios das amostras efetuados pelo Laboratório. No caso de design verifica-se que o modelo representa de forma aceitável as características dos pro-dutos extraídos. Tanto para o caso de Test Run como para os casos reais verifica-se que o modelo representa, na maioria dos casos, as características do destilado e do HVGO nas partes finais das destilações destes produtos, enquanto que o modelo representa as características do LVGO na fase inicial da destilação. Para otimização da coluna de vácuo verificou-se que os parâmetros com maior influência na produção de gasóleo de vácuo são a temperatura da zona de flash da coluna e o caudal de vapor de stripping introduzido no fundo da coluna.

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In order to address and resolve the wastewater contamination problem of the Sines refinery with the main objective of optimizing the quality of this stream and reducing the costs charged to the refinery, a dynamic mass balance was developed nd implemented for ammonia and polar oil and grease (O&G) contamination in the wastewater circuit. The inadequate routing of sour gas from the sour water stripping unit and the kerosene caustic washing unit, were identified respectively as the major source of ammonia and polar substances present in the industrial wastewater effluent. For the O&G content, a predictive model was developed for the kerosene caustic washing unit, following the Projection to Latent Structures (PLS) approach. Comparison between analytical data for ammonia and polar O&G concentrations in refinery wastewater originating from the Dissolved Air Flotation (DAF) effluent and the model predictions of the dynamic mass balance calculations are in a very good agreement and highlights the dominant impact of the identified streams for the wastewater contamination levels. The ammonia contamination problem was solved by rerouting the sour gas through an existing clogged line with ammonia salts due to a non-insulated line section, while for the O&G a dynamic mass balance was implemented as an online tool, which allows for prevision of possible contamination situations and taking the required preventive actions, and can also serve as a basis for establishing relationships between the O&G contamination in the refinery wastewater with the properties of the refined crude oils and the process operating conditions. The PLS model developed could be of great asset in both optimizing the existing and designing new refinery wastewater treatment units or reuse schemes. In order to find a possible treatment solution for the spent caustic problem, an on-site pilot plant experiments for NaOH recovery from the refinery kerosene caustic washing unit effluent using an alkaline-resistant nanofiltration (NF) polymeric membrane were performed in order to evaluate its applicability for treating these highly alkaline and contaminated streams. For a constant operating pressure and temperature and adequate operating conditions, 99.9% of oil and grease rejection and 97.7% of chemical oxygen demand (COD) rejection were observed. No noticeable membrane fouling or flux decrease were registered until a volume concentration factor of 3. These results allow for NF permeate reuse instead of fresh caustic and for significant reduction of the wastewater contamination, which can result in savings of 1.5 M€ per year at the current prices for the largest Portuguese oil refinery. The capital investments needed for implementation of the required NF membrane system are less than 10% of those associated with the traditional wet air oxidation solution of the spent caustic problem. The operating costs are very similar, but can be less than half if reusing the NF concentrate in refinery pH control applications. The payback period was estimated to be 1.1 years. Overall, the pilot plant experimental results obtained and the process economic evaluation data indicate a very competitive solution through the proposed NF treatment process, which represents a highly promising alternative to conventional and existing spent caustic treatment units.