A digestão anaeróbia termofílica é uma opção vantajosa para efluentes descartados a altas temperaturas, além de estimular rotas mais eficientes de produção de H2. No entanto, os resultados da literatura divergem bastante, os rendimentos de H2 são inferiores ao valor teórico possível e poucos estudos avaliaram diferentes configurações para indicar a mais eficiente. Assim, este estudo avaliou a produção de H2 a partir da sacarose em três tipos de reator: reator anaeróbio de fluxo ascendente e manta de lodo (UASB), reator tubular de fluxo ascendente com leito empacotado (TCS) e sem material suporte (TSS), operados a 55°C. Os tempos de detenção hidráulica (TDH) aplicados ao reator UASB foram 12, 6 e 2 h e aos reatores TCS e TSS foram 2 e 0,5 h. Pré-tratamento térmico (100°C por 15 min) foi aplicado ao inóculo metanogênico do UASB e TCS e TSS foram auto inoculados. O efeito de nutrientes e a concentração nutricional ótima para a produção de H2 foram investigados através de ensaios em batelada. Com TDH de 2 h, o material suporte afetou a transferência de massa, resultando em menor teor de H2 no biogás quando presente, porém, maior conversão de sacarose e produção de H2. O pré-tratamento térmico não inibiu a metanogênese, sendo as condições operacionais mais importantes para a seleção dos microrganismos. TCS e TSS com TDH de 0,5 h apresentaram produção de H2 similar e o material suporte afetou apenas as rotas metabólicas. Entre todas as operações, TCS e UASB com TDH de 2 h alcançaram os maiores valores de rendimento de H2 (YH2), respectivamente, 1,99 ± 0,36 e 2,56 ± 0,84 molH2.mol-sac-1, através da via metabólica do etanol. TCS2 também demonstrou estabilidade e, apesar de o U2 ter gerado maiores porcentagens de H2 no biogás, pode ser apontado como o mais eficiente para a produção de H2. A relação C:N:P, Fe+2 e Ni+2 tiveram efeito significativo sobre a produção de H2, e YH2 ótimo foi estimado para concentrações de 4,53 mgFe+2.L-1 e 0,045 mgNi+2.L-1. / The thermophilic anaerobic digestion is a suitable option for wastewater discharged at high temperatures; in addition, it is suitable for more efficient pathways for H2 production. However, the results found in literature have divergences; the H2 yields are lower than the theoretical possible value and only few studies evaluated different types of reactors and defined the more advantageous one. Therefore, this study evaluated H2 production from sucrose in three types of reactor: upflow anaerobic sludge blanket (UASB), upflow tubular reactor with packed-bed (TCS) and without support materials (TSS), operated at 55°C. The hydraulic retention time (HRT) applied to UASB reactor was 12, 6 and 2h and to TCS and TSS was 2 and 0.5h.Thermal pretreatment (at 100°C, for 15 min) was applied to the methanogenic inoculum of UASB and TCS and TSS was inoculated through natural fermentation process. The effect of nutrients and the optimal concentration of t nutrients for H2 production were evaluated through batch assays. At HRT of 2h, the support material affected the mass transferring, leading to lower content of H2 in the biogas when it is used; however, in this condition it was found higher sucrose conversion and H2 production. The operational conditions showed to be more efficient for methanogenesis than pretreatment. TCS and TSS at HRT of 0.5h presented similar H2 production and the support material affected only the metabolic pathways. Among all the conditions assessed, TCS and UASB at HRT of 2h reached the highest values of H2 yield highest YH2, respectively, 1.99 ± 0.36 and 2.56 ± 0.84 molH2.mol-sac-1, through ethanol pathway. TCS2 demonstrated stability production also and, despite the U2 have achieved higher percentage of H2 in biogas, it can be pointed out as more efficient for H2 production. The ratio C:N:P, Fe+2 and Ni+2 showed significant effect on H2 production, and the optimal YH2 was estimated for 4.53 mgFe+2.L-1 e 0.045 mgNi+2.L-1.

No description available.

Modern society has become reliant on battery powered electronic devices such as cell phones and laptop computers. The standard way of recharging these devices is by connecting to a reticulated electricity supply. In situations with no electricity supply some other recharging method is required. Such a possibility is a small, portable, generator based on fuel cell technology, specifically mini-tubular solid oxide fuel cells (MT-SOFC). MT-SOFCs have been developed since the 1990s but there is limited analysis, discussion or research on developing and constructing a portable generator based on MT-SOFC technology. Such a generator, running on a portable gas supply, requires combining the key aspects of cell performance, a heating and fuel reforming system, and cell manifolds. Cell design, fuel type, fuel flow rate, current-collection method and operating temperature all greatly affected MT-SOFCs performance. Segmenting the cathode significantly increased the power output. Maximum power density from an electrolyte supported MT-SOFC was 140 mW/cm2. The partial oxidation reactor (POR) developed provided the required heat to maintain the MT-SOFCs at an operating temperature suitable for generating electricity. The exhaust gas from the POR was a suitable fuel for MT-SOFCs, having sufficient carbon monoxide and hydrogen to generate electricity. Various manifold materials were evaluated including solid metal blocks and folded sheet metal. It was found that manifolds made from easily worked alumina fibre board decreased the thermal stresses and therefore the fracture rate of the MT-SOFCs. The final prototype developed comprised a partial oxidation reactor and MT-SOFCs mounted in alumina fibre board manifolds within a well-insulated enclosure, which could be run on LPG. Calculated efficiency of the final prototype was 4%. If all the carbon monoxide and hydrogen produced by the partial oxidation reactor were converted to electrical energy, efficiency would increase to 39%. Under ideal conditions, efficiency would be 78%. Efficiency of the prototype can be improved by increasing the fuel and oxygen utilisation ratios, ensuring heat from the exhaust gases is transferred to the incoming gases, and improving the methods for collecting current at both the anode and cathode.

published_or_final_version / abstract / Civil Engineering / Doctoral / Doctor of Philosophy

published_or_final_version / Civil Engineering / Doctoral / Doctor of Philosophy

Haloalkenes were shown to react with cysteine, N-acetyl cysteine, or glutathione to form halogenated vinylthio (HVT) or saturated conjugates. When HVT were administered iv to rabbits, active transport in the renal tubules was inhibited 50% at doses as low as 20 mg/kg within 1 hr after dosing. There was sloughing of the renal brush border membrane with the injury progressing to a specific renal tubular necrosis of the S₃ segment. In vitro studies with renal tubules found that the HVT produced a dose-response related inhibition of acid/base transport, with complete inhibition of transport occurring at 1 mM. The cysteine conjugate synthesized from trichloroethylene, DCVC, inhibited tubular active transport 60 min after in vivo dosing (20-100 mg/kg), 45 min after exposure in the isolated perfused kidney (0.01-1 mM) and 15 min after incubation with isolated tubules (0.01-1 mM). All HVT conjugates had a similar potency with regard to transport inhibition in isolated tubules, with complete inhibition occurring at 1 mM within 15 min for cysteine conjugates compared to 45-60 min for the N-acetyl cysteine or glutathione conjugates. These latter conjugates are thought to be bioactivated to the cysteine conjugate prior to transport inhibition. Inhibition of tubular (gamma)-glutamyl transpeptidase by 1 mM AT-125 or 20 mM serine/borate prevented the inhibition of acid/base transport by the glutathione conjugate. In addition, the sequential formation of glutamate, glycine and the vinyl cysteine conjugate after tubule incubation with the glutathione conjugate provides further evidence for this bioactivation. The cysteine conjugates are thought to be further metabolized in tubules to a toxic intermediate by a brush border localized enzyme, C-S lyase. The inhibitor effect of this intermediate on acid/base transport is reversed in the presence of, or subsequent addition of, 6 mM exogenous glutathione. These studies provide further evidence for the nephrotoxicity of HVT, and formation of the nephrotoxic cysteine conjugates from glutathione and cysteine conjugates. The formation of saturated conjugates from CTFE was also demonstrated. These saturated and/or unsaturated conjugates may be responsible for haloalkene-induced nephrotoxicity.

The performance of peristaltic pumps is mainly governed by their tubing or hose materials. Research and development in this area is therefore very important for peristaltic pump manufacturers to keep in front of the competition and to open up new applications to enable further market penetration. Another aspect of this is of course price; performance and cost have to be in balance. As an approach to fabricate a new tube material, the field of negative Poisson's ratio (or: auxetic) materials is explored. The combined deformations of tensile, compression and shear in a peristaltic pump tube may well benefit from the specific characteristics of auxetic materials. Materials can be designed to keep their dimensions constant in directions perpendicular to an applied load. This is referred to as “auxetic balancing”. Finite element modelling shows that lowering the Poisson's ratio will rapidly decrease the maximum stresses in the cross-section of an occluded tube. Optimum values for the Poisson's ratio are found to be between −0.1 and +0.1, preferentially being 0. The re-entrant honeycomb structure is selected for initial trials, but manufacturing of this structure at the desired dimension proved to be too difficult at this time. Instead, electrospun nanofibre membranes are selected as the reinforcement structure. A liquid silicone elastomer is used as the matrix material. Key characteristics for the new material are derived from baseline test results on existing tubing. Laminates are manufactured from electrospun nylon6 nanofibre membranes coated with a liquid silicone rubber. Compression moulding is used to cure the nylon6-silicone rubber laminate, to give two effects: it ensures impregnation of the membrane and the compression deforms the nanofibre structure in such a way that it will become auxetic through-the-thickness. Flat sheet laminates of 2 mm thickness are manufactured with 14 layers of reinforcement. A reinforcing effect and substantial lowering of the through-the-thickness Poisson's ratio is observed for the laminates at low strains. At higher strains (>50%) the effect of the reinforcement diminishes and the Poisson's ratio of the laminate and pure silicone rubber equalises. Finally, tubular laminates are manufactured and the resulting tubes are tested in a peristaltic pump with some promising results (>1 million occlusions before failure). Tube performance is not yet at the required level, but with further optimisation of the laminating process, mould design and (post-)curing large steps forward can be made.

With 500,000 coronary artery bypass procedures performed each year in the United States, and only one-third of patients possessing suitable autologous grafts, there is a clinical need for tissue engineered blood vessels (TEBVs). The overall goal of this project was to develop a one- step approach to rapidly produce entirely cell- derived tubular tissue constructs without scaffold materials. To achieve this goal, we developed "centritubing"-- a system based on applying centrifugal force to suspended cells to create a tube-shaped cellular aggregate. Briefly, rat aortic smooth muscle cells were injected into cylindrical polycarbonate spinning chambers and then spun to apply centrifugal force, which pelletted the cells on the inner wall of the chamber. After three days in culture with growth medium, the cells remodeled to form tissue tubes. In previous work we have shown, in principle, that centritubing produces tubular constructs, however tissue tube production was not consistently achieved. The first objective of this study was to develop modifications to the centritubing device that would lead to consistent lumen diameter, rapid cellular aggregation into a tube construct, and an improved success rate of tube formation. The second objective was to investigate cellular parameters that contribute to tubular tissue construct formation using centritubing. Prior to changes in manufacturing of the centritubing device and culture system, the success rate of centritubing was inconsistent. After these changes, the success rate of tubular construct formation improved to 85% (11/13). Noteworthy modifications to the centritubing device included the addition of a central mandrel as a substrate for tissue contraction, development of a smoother seeding surface, and manufacture of a reusable culture chamber. The results of this study support the proof of concept for centritubing as a device for rapid production of tubular tissue constructs and provide insight for future progress using the centritubing methodology.

Made available in DSpace on 2014-06-12T17:36:00Z (GMT). No. of bitstreams: 2 arquivo2097_1.pdf: 4723187 bytes, checksum: bcc3c1be474970fe1a53f1da46de7552 (MD5) license.txt: 1748 bytes, checksum: 8a4605be74aa9ea9d79846c1fba20a33 (MD5) Previous issue date: 2009 / Nas indústrias de processo, os diversos equipamentos formam uma cadeia contínua, através da qual circulam os fluidos, o meio de ligação entre os mesmo se dá atarvés de tubulações que são consideradas como equipamentos de processo. A falta ou paralisação de um único equipamento, sem que tenha sido programa, pode gerar perdas financeiras em grande escala. Neste ambiente, as tubulações são responsáveis pela condução dos fluidos, as quais operam em muitos casos em severas condições de serviço. Na ocasião da montagem, as tubulações passam por processos de soldagem nos seus diversos métodos de ligação, durante o processo de soldagem são geradas zonas de aquecimento localizadas nas juntas onde o material do tubo fica sujeito a variações na sua microestrutura, o que gera mudanças nas suas propriedades. O processo de soldagem mais utilizado na soldagem de tubulações nas montagens industriais é o da soldagem a arco elétrico com eletrodo revestido. Este trabalho apresenta o resultado do estudo das propriedades mecânicas e estruturais de juntas de tubos soldadas com arame tubular. Para tanto, utilizou-se tubos confeccionados em aço ASTM A106 Gr B, recomendado para o transporte de fluidos em alta temperatura, soldado com o processo de soldagem por arco elétrico com Arame Tubular Protegido. As soldas de raiz foram feitas com dois diferentes processos: TIG e Arame Tubular, quando se utilizou arame tubular na raiz, este foi feito com o mesmo material de enchimento e acabamento. As soldas de enchimento e acabamento foram feitas com dois tipos de arame tubular, um rutílico e outro metal cored . Foram realizados ensaios de microdureza e de tração, e análise microestrutural e macroestrutural das juntas soldadas para verificação das suas possíveis variações. Os resultados evidenciaram variações nas propriedades das juntas soldadas quando se realiza a solda nas diferentes amperagens adotadas neste trabalho, porém mostrou-se possível a utilização do processo estudado em pequenas juntas de peças que possam vir a serem fabricadas em canteiros de obra

Concrete filled steel tubular (CFST) columns are widely used in building and infrastructure projects throughout the world.Compared with other form of construction CFST columns offer superior structural performance and speed and ease of construction.Design procedures and recommendations provided in most of the design codes are often tedious and complex. There have been attempts to simplify the design procedure by providing a simplified expression to predict the capacity of a CFST under a general loading condition.In this thesis a rigorous analysis procedure was presented for the analysis of CFST beam-columns under general loading conditions.All the analytical results were verified by comparisons with the available test results and current ACI, AISC AND Eurocode 4 design codes. The comparisons demonstrated that the proposed numerical equations are accurate, and slightly conservative. Based on the numerical analysis, a simple and easy to follow calculation procedure was proposed for design of CFST columns under either uniaxial or biaxial bending moment and axial load. / Doctor of Philosophy (PhD)