5 resultados para stripping chronopotentiometry
em Repositório Científico do Instituto Politécnico de Lisboa - Portugal
Resumo:
O presente trabalho descreve o estudo da viabilidade económica de implementar um processo de absorção química com monoetanolamina (MEA) numa central termoeléctrica, visando a captura de CO2 dos gases de exaustão da mesma, dado que na indústria, o sector de produção de energia eléctrica é o principal responsável pela emissão de CO2 para a atmosfera. A central em foco foi a TER (Central Termoeléctrica do Ribatejo) devido à quantidade de gases emitidos e ao teor em CO2 dos mesmos, além de ser a responsável por cerca de 18% da energia eléctrica em Portugal. O processo em causa ocorre em pós-combustão, dado tratar-se de uma central já existente, e engloba a absorção química com MEA, seguida de stripping, com remoção do CO2 e recirculação da MEA. Este sistema foi testado recorrendo a um modelo de simulação desenvolvido por T. Greer, na sua tese de mestrado ao tema “Modeling and simulation of post combustion CO2 capturing” com base em Matlab. De acordo com o disposto sobre o Comércio Europeu de Licenças de Emissão (CELE), para o período de 2008-2012, foi atribuído à TER um limite de emissão de 1.423.103 ton CO2/ano. Sendo esta responsável pela emissão anual de cerca de 2X106 toneladas, determinou-se um encargo de 17.277.000 € anuais por incumprimento. Os custos de implementação deste processo estimam-se, para um período de amortização de 5 anos, em 6.546.758€, e permitiria a captação de 78,7% do CO2 emitido. As taxas respeitantes ao incumprimento ficariam reduzidas a 13.597.020€; o que significa que, com a implementação desta tecnologia, se conseguirá uma economia de: 17.277.000 - 13.597.020 = 3.679.980 €/ano. Estes valores foram calculados de acordo com o valor cotado da tonelada de CO2 para 2008 de 30 euros/ton. No período de amortização considerado, 5 anos, obtém-se uma economia de 18.399.900 €, sendo possível amortizar totalmente o investimento efectuado com a unidade de captura de CO2 sendo economicamente viável a sua implementação.
Resumo:
Nickel-copper metallic foams were electrodeposited from an acidic electrolyte, using hydrogen bubble evolution as a dynamic template. Their morphology and chemical composition was studied by scanning electron microscopy and related to the deposition parameters (applied current density and deposition time). For high currents densities (above 1 A cm(-2)) the nickel-copper deposits have a three-dimensional foam-like morphology with randomly distributed nearly-circular pores whose walls present an open dendritic structure. The nickel-copper foams are crystalline and composed of pure nickel and a copper-rich phase containing nickel in solid solution. The electrochemical behaviour of the material was studied by cyclic voltammetry and chronopotentiometry (charge-discharge curves) aiming at its application as a positive electrode for supercapacitors. Cyclic voltammograms showed that the Ni-Cu foams have a pseudocapacitive behaviour. The specific capacitance was calculated from charge-discharge data and the best value (105 F g(-1) at 1 mA cm(-2)) was obtained for nickel-copper foams deposited at 1.8 A cm(-2) for 180 s. Cycling stability of these foams was also assessed and they present a 90 % capacitance retention after 10,000 cycles at 10 mA cm(-2).
Resumo:
Nickel-copper metallic foams were electrodeposited from an acidic electrolyte, using hydrogen bubble evolution as a dynamic template. Their morphology and chemical composition was studied by scanning electron microscopy and related to the deposition parameters (applied current density and deposition time). For high currents densities (above 1 A cm(-2)) the nickel-copper deposits have a three-dimensional foam-like morphology with randomly distributed nearly-circular pores whose walls present an open dendritic structure. The nickel-copper foams are crystalline and composed of pure nickel and a copper-rich phase containing nickel in solid solution. The electrochemical behaviour of the material was studied by cyclic voltammetry and chronopotentiometry (charge-discharge curves) aiming at its application as a positive electrode for supercapacitors. Cyclic voltammograms showed that the Ni-Cu foams have a pseudocapacitive behaviour. The specific capacitance was calculated from charge-discharge data and the best value (105 F g(-1) at 1 mA cm(-2)) was obtained for nickel-copper foams deposited at 1.8 A cm(-2) for 180 s. Cycling stability of these foams was also assessed and they present a 90 % capacitance retention after 10,000 cycles at 10 mA cm(-2).
Resumo:
Copper iron (Cu-Fe) 3D porous foams for supercapacitor electrodes were electrodeposited in the cathodic regime, on stainless steel current collectors, using hydrogen bubbling dynamic template. The foams were prepared at different current densities and deposition times. The foams were submitted to thermal conditioning at temperatures of 150 and 250 degrees C. The morphology, composition and structure of the formed films were studied by SEM, EDS and XRD, respectively. The electrochemical behaviour was studied by cyclic voltammetry, electrochemical impedance spectroscopy and chronopotentiometry. The morphology of the 3D Cu-Fe foams is sensitive to the electrodeposition current and time. The increase of the current density produces a denser, larger and more ramified dendritic structure. Thermal conditioning at high temperature induces a coarser grain structure and the formation of copper oxides, which affect the electrochemical behaviour. The electrochemical response reveals the presence of various redox peaks assigned to the oxidation and reduction of Cu and Fe oxides and hydroxides in the foams. The specific capacitance of the 3D Cu Fe foams was significantly enhanced by thermal conditioning at 150 degrees C. The highest specific capacitance values attained 297 Fg(-1) which are much above the ones typically observed for single Cu or Fe Oxides and hydroxides. These values highlight a synergistic behaviour resulting from the combination of Cu and Fe in the form of nanostructured metallic foams. Moreover, the capacitance retention observed in an 8000 charge/discharge cycling test was above 66%, stating the good performance of these materials and its enhanced electrochemical response as supercapacitor negative electrodes. (C) 2014 Elsevier B.V. All rights reserved.
Resumo:
CO2 capture from gaseous effluents is one of the great challenges faced by chemical and environmental engineers, as the increase in CO2 levels in the Earth atmosphere might be responsible for dramatic climate changes. From the existing capture technologies, the only proven and mature technology is chemical absorption using aqueous amine solutions. However, bearing in mind that this process is somewhat expensive, it is important to choose the most efficient and, at the same time, the least expensive solvents. For this purpose, a pilot test facility was assembled and includes an absorption column, as well as a stripping column, a heat exchanger between the two columns, a reboiler for the stripping column, pumping systems, surge tanks and all necessary instrumentation and control systems. Some different aquous amine solutions were tested on this facility and it was found that, from a set of six tested amines, diethanol amine is the one that turned out to be the most economical choice, as it showed a higher CO2 loading capacity (0.982 mol of CO2 per mol of amine) and the lowest price per litre (25.70 ¤/L), even when compared with monoethanolamine, the benchmark solvent, exhibiting a price per litre of 30.50 ¤/L.