Turbomáquinas térmicas: 1. Turbomáquinas térmicas. 2. Estudio y diseño de turbinas de gas. 3. Problemas

Contenido: - Instalaciones de turbina de gas. - Análisis de los procesos termodinámicos. - Conceptos básicos para el análisis de turbinas de gas: a) Instalación de turbina de gas. b) Turbina como máquina térmica. - Análisis mediante el software Turgas.

Vulnerabilidade socioambiental dos manguezais de Garapuá, Cairu/BA frente à inserção da indústria petroleira.

Manguezais são ecossistemas marinhos costeiros que ocorrem nas regiões tropicais e subtropicais do globo. A associação desses ambientes a formações recifais é restrita, particularmente no Brasil, onde se destaca a ilha de Tinharé, na costa sul do estado da Bahia, não só pela ocorrência desse sistema manguezal-recifes, mas também pelo desenvolvimento estrutural da floresta e pela atividade produtiva de mariscagem exercida pela população do povoado de Garapuá. Apesar da proximidade de Morro de São Paulo, atrator turístico internacional, este povoado experimentava certo isolamento socioeconômico até a chegada da indústria do petróleo que, em função de suas potencialidades e riscos, tensionou a vida da comunidade local. Este estudo tem por objetivo analisar a vulnerabilidade socioambiental dos manguezais adjacentes à Garapuá, Cairu-BA, frente a inserção da indústria petrolífera na região, a partir da caracterização estrutural das florestas de mangue e da caracterização social do povoado de Garapuá e, particularmente, das marisqueiras usuárias deste ecossistema. As abordagens metodológicas utilizadas podem ser classificadas como pesquisas quantitativas, empregadas no levantamento fitossociológico, e qualitativas, utilizadas a partir de observações de campo e entrevistas, além de levantamentos bibliográficos, para elaboração das análises sociais. Os resultados indicam florestas de mangue de porte variável, em bom estado de conservação, com altura média das dez árvores mais altas entre 2,40,2 metros (estação 7) e 22,71,1 metros (estação 29), geralmente dominadas por Rhizophora mangle (38 das 52 estações de amostragem). A partir da caracterização estrutural foi realizado teste estatístico de agrupamento que, aliado a aspectos da arquitetura das árvores, permitiu a classificação das florestas em 12 Tipos Estruturais. As análises relativas à vulnerabilidade ambiental fundamentaram-se nos aspectos de sensibilidade e na posição fisiográfica ocupada por cada Tipo de floresta e identificaram níveis distintos de vulnerabilidade a derramamentos de óleo. Com relação aos aspectos sociais, as informações sobre os sistemas socioeconômicos e culturais relacionados à saúde, à educação, às práticas produtivas e à geração de renda, ao transporte, à religião e à organização social, como um todo, evidenciaram vulnerabilidades frente à inserção da indústria do petróleo, apontando as marisqueiras como o segmento mais suscetível a vivenciar os riscos e os impactos desse empreendimento no local. A inserção da indústria do petróleo neste contexto socioambiental representa aumento de riscos e, consequentemente, de vulnerabilidade socioambiental, na medida em que o diálogo estabelecido entre empreendedor e população se apresenta de forma assimétrica, dificultando a participação da população local, sobretudo dos mais excluídos que, nesse caso, são representados pelos usuários dos manguezais.

Advanced Reaction Systems for Hydrogen Production

[EN] This PhD work started in March 2010 with the support of the University of the Basque Country (UPV/EHU) under the program named “Formación de Personal Investigador” at the Chemical and Environmental Engineering Department in the Faculty of Engineering of Bilbao. The major part of the Thesis work was carried out in the mentioned department, as a member of the Sustainable Process Engineering (SuPrEn) research group. In addition, this PhD Thesis includes the research work developed during a period of 6 months at the Institut für Mikrotechnik Mainz GmbH, IMM, in Germany. During the four years of the Thesis, conventional and microreactor systems were tested for several feedstocks renewable and non-renewable, gases and liquids through several reforming processes in order to produce hydrogen. For this purpose, new catalytic formulations which showed high activity, selectivity and stability were design. As a consequence, the PhD work performed allowed the publication of seven scientific articles in peer-reviewed journals. This PhD Thesis is divided into the following six chapters described below. The opportunity of this work is established on the basis of the transition period needed for moving from a petroleum based energy system to a renewable based new one. Consequently, the present global energy scenario was detailed in Chapter 1, and the role of hydrogen as a real alternative in the future energy system was justified based on several outlooks. Therefore, renewable and non-renewable hydrogen production routes were presented, explaining the corresponding benefits and drawbacks. Then, the raw materials used in this Thesis work were described and the most important issues regarding the processes and the characteristics of the catalytic formulations were explained. The introduction chapter finishes by introducing the concepts of decentralized production and process intensification with the use of microreactors. In addition, a small description of these innovative reaction systems and the benefits that entailed their use were also mentioned. In Chapter 2 the main objectives of this Thesis work are summarized. The development of advanced reaction systems for hydrogen rich mixtures production is the main objective. In addition, the use and comparison between two different reaction systems, (fixed bed reactor (FBR) and microreactor), the processing of renewable raw materials, the development of new, active, selective and stable catalytic formulations, and the optimization of the operating conditions were also established as additional partial objectives. Methane and natural gas (NG) steam reforming experimental results obtained when operated with microreactor and FBR systems are presented in Chapter 3. For these experiments nickel-based (Ni/Al2O3 and Ni/MgO) and noble metal-based (Pd/Al2O3 and Pt/Al2O3) catalysts were prepared by wet impregnation and their catalytic activity was measured at several temperatures, from 973 to 1073 K, different S/C ratios, from 1.0 to 2.0, and atmospheric pressure. The Weight Hourly Space Velocity (WHSV) was maintained constant in order to compare the catalytic activity in both reaction systems. The results obtained showed a better performance of the catalysts operating in microreactors. The Ni/MgO catalyst reached the highest hydrogen production yield at 1073 K and steam-to-carbon ratio (S/C) of 1.5 under Steam methane Reforming (SMR) conditions. In addition, this catalyst also showed good activity and stability under NG reforming at S/C=1.0 and 2.0. The Ni/Al2O3 catalyst also showed high activity and good stability and it was the catalyst reaching the highest methane conversion (72.9 %) and H2out/CH4in ratio (2.4) under SMR conditions at 1073 K and S/C=1.0. However, this catalyst suffered from deactivation when it was tested under NG reforming conditions. Regarding the activity measurements carried out with the noble metal-based catalysts in the microreactor systems, they suffered a very quick deactivation, probably because of the effects attributed to carbon deposition, which was detected by Scanning Electron Microscope (SEM). When the FBR was used no catalytic activity was measured with the catalysts under investigation, probably because they were operated at the same WHSV than the microreactors and these WHSVs were too high for FBR system. In Chapter 4 biogas reforming processes were studied. This chapter starts with an introduction explaining the properties of the biogas and the main production routes. Then, the experimental procedure carried out is detailed giving concrete information about the experimental set-up, defining the parameters measured, specifying the characteristics of the reactors used and describing the characterization techniques utilized. Each following section describes the results obtained from activity testing with the different catalysts prepared, which is subsequently summarized: Section 4.3: Biogas reforming processes using γ-Al2O3 based catalysts The activity results obtained by several Ni-based catalysts and a bimetallic Rh-Ni catalyst supported on magnesia or alumina modified with oxides like CeO2 and ZrO2 are presented in this section. In addition, an alumina-based commercial catalyst was tested in order to compare the activity results measured. Four different biogas reforming processes were studied using a FBR: dry reforming (DR), biogas steam reforming (BSR), biogas oxidative reforming (BOR) and tri-reforming (TR). For the BSR process different steam to carbon ratios (S/C) from 1.0 to 3.0, were tested. In the case of BOR process the oxygen-to-methane (O2/CH4) ratio was varied from 0.125 to 0.50. Finally, for TR processes different S/C ratios from 1.0 to 3.0, and O2/CH4 ratios of 0.25 and 0.50 were studied. Then, the catalysts which achieved high activity and stability were impregnated in a microreactor to explore the viability of process intensification. The operation with microreactors was carried out under the best experimental conditions measured in the FBR. In addition, the physicochemical characterization of the fresh and spent catalysts was carried out by Inductively Coupled Plasma Atomic Emission Spectroscopy (ICP-AES), N2 physisorption, H2 chemisorption, Temperature Programmed Reduction (TPR), SEM, X-ray Photoelectron Spectroscopy (XPS) and X-ray powder Diffraction (XRD). Operating with the FBR, conversions close to the ones predicted by thermodynamic calculations were obtained by most of the catalysts tested. The Rh-Ni/Ce-Al2O3 catalyst obtained the highest hydrogen production yield in DR. In BSR process, the Ni/Ce-Al2O3 catalyst achieved the best activity results operating at S/C=1.0. In the case of BOR process, the Ni/Ce-Zr-Al2O3 catalyst showed the highest reactants conversion values operating at O2/CH4=0.25. Finally, in the TR process the Rh-Ni/Ce-Al2O3 catalyst obtained the best results operating at S/C=1.0 and O2/CH4=0.25. Therefore, these three catalysts were selected to be coated onto microchannels in order to test its performance under BOR and TR processes conditions. Although the operation using microreactors was carried out under considerably higher WHSV, similar conversions and yields as the ones measured in FBR were measured. Furthermore, attending to other measurements like Turnover Frequency (TOF) and Hydrogen Productivity (PROD), the values calculated for the catalysts tested in microreactors were one order of magnitude higher. Thus, due to the low dispersion degree measured by H2-chemisorption, the Ni/Ce-Al2O3 catalyst reached the highest TOF and PROD values. Section 4.4: Biogas reforming processes using Zeolites L based catalysts In this section three type of L zeolites, with different morphology and size, were synthesized and used as catalyst support. Then, for each type of L zeolite three nickel monometallic and their homologous Rh-Ni bimetallic catalysts were prepared by the wetness impregnation method. These catalysts were tested using the FBR under DR process and different conditions of BSR (S/C ratio of 1.0 and 2.0), BOR (O2/CH4 ratio of 0.25 and 0.50) and TR processes (at S/C=1.0 and O2/CH4=0.25). The characterization of these catalysts was also carried out by using the same techniques mentioned in the previous section. Very high methane and carbon dioxide conversion values were measured for almost all the catalysts under investigation. The experimental results evidenced the better catalytic behavior of the bimetallic catalysts as compared to the monometallic ones. Comparing the catalysts behavior with regards to their morphology, for the BSR process the Disc catalysts were the most active ones at the lowest S/C ratio tested. On the contrary, the Cylindrical (30–60 nm) catalysts were more active under BOR conditions at O2/CH4=0.25 and TR processes. By the contrary, the Cylindrical (1–3 µm) catalysts showed the worst activity results for both processes. Section 4.5: Biogas reforming processes using Na+ and Cs+ doped Zeolites LTL based catalysts A method for the synthesis of Linde Type L (LTL) zeolite under microwave-assisted hydrothermal conditions and its behavior as a support for heterogeneously catalyzed hydrogen production is described in this section. Then, rhodium and nickel-based bimetallic catalysts were prepared in order to be tested by DR process and BOR process at O2/CH4=0.25. Moreover, the characterization of the catalysts under investigation was also carried out. Higher activities were achieved by the catalysts prepared from the non-doped zeolites, Rh-Ni/D and Rh-Ni/N, as compared to the ones supported on Na+ and Cs+ exchanged supports. However, the differences between them were not very significant. In addition, the Na+ and Cs+ incorporation affected mainly to the Disc catalysts. Comparing the results obtained by these catalysts with the ones studied in the section 4.4, in general worst results were achieved under DR conditions and almost the same results when operated under BOR conditions. In Chapter 5 the ethylene glycol (EG) as feed for syngas production by steam reforming (SR) and oxidative steam reforming (OSR) was studied by using microchannel reactors. The product composition was determined at a S/C of 4.0, reaction temperatures between 625°C and 725°C, atmospheric pressure and Volume Hourly Space Velocities (VHSV) between 100 and 300 NL/(gcath). This work was divided in two sections. The first one corresponds to the introduction of the main and most promising EG production routes. Then, the new experimental procedure is detailed and the information about the experimental set-up and the measured parameters is described. The characterization was carried out using the same techniques as for the previous chapter. Then, the next sections correspond to the catalytic activity and catalysts characterization results. Section 5.3: xRh-cm and xRh-np catalysts for ethylene glycol reforming Initially, catalysts with different rhodium loading, from 1.0 to 5.0 wt. %, and supported on α-Al2O3 were prepared by two different preparation methods (conventional impregnation and separate nanoparticle synthesis). Then, the catalysts were compared regarding their measured activity and selectivity, as well as the characterization results obtained before and after the activity tests carried out. The samples prepared by a conventional impregnation method showed generally higher activity compared to catalysts prepared from Rh nanoparticles. By-product formation of species such as acetaldehyde, ethane and ethylene was detected, regardless if oxygen was added to the feed or not. Among the catalysts tested, the 2.5Rh-cm catalyst was considered the best one. Section 5.4: 2.5Rh-cm catalyst support modification with CeO2 and La2O3 In this part of the Chapter 5, the catalyst showing the best performance in the previous section, the 2.5Rh-Al2O3 catalyst, was selected in order to be improved. Therefore, new Rh based catalysts were designed using α-Al2O3 and being modified this support with different contents of CeO2 or La2O3 oxides. All the catalysts containing additives showed complete conversion and selectivities close to the equilibrium in both SR and OSR processes. In addition, for these catalysts the concentrations measured for the C2H4, CH4, CH3CHO and C2H6 by-products were very low. Finally, the 2.5Rh-20Ce catalyst was selected according to its catalytic activity and characterization results in order to run a stability test, which lasted more than 115 hours under stable operation. The last chapter, Chapter 6, summarizes the main conclusions achieved throughout this Thesis work. Although very high reactant conversions and rich hydrogen mixtures were obtained using a fixed bed reaction system, the use of microreactors improves the key issues, heat and mass transfer limitations, through which the reforming reactions are intensified. Therefore, they seem to be a very interesting and promising alternative for process intensification and decentralized production for remote application.

Remediação de solos e lençóis freáticos em postos de gasolina via processo de fenton: estudo de caso

Alguns cientistas ambientais prevêem que a poluição dos solos será um dos maiores legados com grandes impactos para as gerações futuras, pois atualmente ainda existe desconhecimento das fontes poluidoras e da sua extensão. O Brasil, devido a sua extensão territorial, suas bacias hidrográficas, número de postos de abastecimentos e controles ambientais ainda ineficazes, está muito exposto a esse tipo de poluição. Atualmente, há no Brasil mais de 34.300 postos de combustíveis, com volume de 65.000.000 m3 de gasolina e diesel consumidos anualmente, conforme dados da Agência Nacional do Petróleo Gás Natural e Biocombustíveis , ANP, em 2008. Sendo assim, a exposição e contaminação dos solos e dos lençóis freáticos com constituintes aromáticos do diesel e gasolina torna-se um sério problema ambiental. Dentro deste grupo, encontram-se o benzeno, tolueno, xileno, conhecido como BTEX e os hidrocarbonetos policíclicos aromáticos, conhecido como PAH. Este trabalho tem como objetivo estudar a remediação in-situ de um posto de combustíveis na região do ABC Paulista, no Estado de São Paulo. Aplicando-se a técnica de Processo Oxidativo Avançado via reagente de Fenton (H2O2 + Fe2+ → Fe3+ + OH- + OH . ), o radical hidroxila gerado mineraliza compostos aromáticos, decompondo-os definitivamente. Amostras de água do posto em estudo apresentavam elevados teores de BTEX e PAH, 2,58 mg.L-1 e 0,298 mg.L-1 respectivamente, estando em níveis não tolerados pelo órgão ambiental paulista CETESB sendo necessária a intervenção para tratamento da área. Com os níveis de poluentes e o perfil hidrogeológico identificados, a remediação foi iniciada com injeções no solo de peróxido de hidrogênio a 8%v.v, FeSO4 a 0,40 mg.L-1 e solução à base de NPK (nitrogênio, fósforo e nitrogênio) a 100 mg.L-1 como nutrientes para os microorganismos do solo. Estes valores são provenientes de experimentos anteriores e tratamentos já realizados. Foram conduzidas campanhas de injeção trimestrais com 100 litros desta solução completa como reagente , e medições trimestrais de BTEX, PAH e outros parâmetros de controle, que foram indicando o sucesso do tratamento. Após 18 meses o local foi considerado tratado pelo órgão ambiental, onde monitoramentos semestrais estão em continuidade para garantir o resultado do tratamento e das ações corretivas. Assim, o estudo real da remediação de solos contaminados com os poluentes orgânicos via processo de Fenton, com concentração de H2O2 a 8%v/v, e FeSO4 a 0,40 mg.L-1 demonstrou-se uma técnica de sucesso. O entendimento dos resultados da remediação, mesmo sujeitos aos fenômenos naturais, como intempéries e chuvas, é uma experiência grande, pois por mais reais que simulações em laboratório possam ser, é muito difícil incluir nestes sistemas, as variações que um tratamento real está exposto

Preparation, characterization and gas sensing properties of high soluble metal (II) phthalocyanine thin films by spin-coating method

Three novel metal (II) phthalocyanine complexes were synthesized by cyclic tetramerisation reaction of a dicyano benzene component and different metal ions (Pd2+, Co2+, Zn2+). The structure of complexes was confirmed by elemental analysis, mass and IR spectrum. The excellent solubility of the complexes in benzene enabled us to obtain films by a spin-coating method. The films were characterized by IR, electronic spectral and AFM. The gas sensing properties to NO2 of the metal (II) phthalocyanine complex films were studied. In addition, the effects of different metal ions and the gas sensing temperature on the sensing properties were studied. (C) 2005 Elsevier B.V. All rights reserved.

Preparation, characterization and gas sensing properties of lead tetra-(tert-butyl)-5,10,1 5,20-tetraazaporphyrin spin-coating films

A spin-coated film of lead tetra-(tert-butyl)-5,10,15,20-tetraazaporphyrin complex (PbTAP(t-Bu)(4)) was obtained and characterized by IR spectra, absorption spectra and atomic force microscopy. The response and recovery characteristics of the film to NH3, NO2 and C2H5OH vapor were investigated at room temperature. In addition, the reversibility and stability of the film to NH3 were also studied. The results indicate that the PbTAP(t-Bu)(4) derivative can be exploited as an NH3 sensor at room temperature. (c) 2007 Elsevier B.V. All rights reserved.

Preparation, characterization and gas sensing properties of nickel octa-iso-pentyloxynaphthalocyanine spin-coating films

Spin-coated films of nickel 1,6,10,15,19,24,28,33-octa-iso-pentyloxy-2,3-naphthalocyanine complex were obtained and characterized by UV-vis absorption spectroscopy. A linear relationship between the absorbance and solution concentration was observed. Low concentration solutions could afford smooth and homogeneous film surfaces as indicated by atomic force microscopy. The film structure was studied by small angle X-ray diffraction. The films were used for NO2 sensing experiments. The results indicate that the elevation of sensing temperature can shorten the response time and increase recovery ratio and response magnitude of the sensing films. High NO2 concentration can also shorten response time. (C) 2008 Elsevier B.V. All rights reserved.