Redução dos riscos de operação na montagem de mancais em cilindros de laminação em uma usina siderúrgica

The increasing concerns about the health and safety is significantly changing the costeffective management of labor, also becoming an important tool in the pursuit of quality. In this context the present work makes a studyin a steel mill, to determine an action plan with the goal of reducing the risk of injury during handling and setting up bearings in a workshop of rolling mill rolls. The study is structured through the Method of Analysis and Troubleshooting, and quality tools. The definition of the action plan has brought lowcost measures that seek to solve the problem, eliminating the possibility of fatality or inability to employees

Análise de cilindros de paredes grossas através do método dos elementos finitos

Have long studied the distribution of stresses in the cylinder. When this thickness is less than or equal to 10% of the inner radius is possible to consider a uniform distribution along the thickness of the tube. However, when the thickness is greater than 10% of the inner radius is necessary to consider the theory of thick-walled cylinders. This theory shows that when the thickness increases on the radius, the stresses do not act uniformly. The objective of this study is to determine the maximum stresses in thick-walled cylinders by comparing the results obtained by the theory of elasticity and the finite element method

Influência do tratamento térmico de homogeneização na microestrutura de um aço utilizado na fabricação de cilindros de laminação para trabalho a frio

Pós-graduação em Engenharia Mecânica - FEG

Avaliação da usinabilidade de cilindros para laminação de tiras a quente

Pós-graduação em Engenharia Mecânica - FEG

Desgaste adhesivo (scuffing) en camisas de cilindros y aros de pistón de motores diesel lentos de dos tiempos

[ES] En este trabajo se describe el desgaste adhesivo (scuffing) que representa la más severa de las agresiones a la que se ven expuestos aros de pistón y camisas de cilindro de motores diésel lentos de dos tiempos aplicados a la generación eléctrica, al quemar combustibles de bajo contenido en azufre. Al afectar simultáneamente, a estos dos elementos básicos de la cámara de combustión, repercute negativamente tanto en la continuidad del servicio del motor, como en los costes asociados a la restitución de las condiciones nominales de trabajo.

Moldeo de cilindros de laminación

Se trata de los procedimientos seguidos en la fabricación y moldeo de cilindros de laminación

Avaliação tribológica de novas modificações superficiais para cilindros de laminação a frio

The present work analyzed the tribological behavior of coatings/surface modifications traditionally used in cold rolling mill rolls and new coatings/surface modificationswith potential to replace the carcinogenic hard chrome. The study started with identification of wear mechanisms occurring in real coldrollingmill rolls. Due the high cost and dimensions of the rolls, thereplication technique was used. Replicas were obtained from 4 different rolling millBrazilian companies before and after a normal rolling campaign. Initial sliding tests were conducted using spherical and cylindrical counter bodies in order to verifywhichtribological conditions allowed to reproduce the wear mechanisms found in the replicas. These tests indicated the use of reciprocating sliding tests with cylindrical counter bodies (line contact), normal load of 100 N, and test times of and 1 h and 5 h. Different surface modifications were carried out on samples produced from a fragment of a rolling mill roll. The specimens were heat treated and ground on both sides. After, some specimens were surface textured by electrical discharge texturing (EDT). For both groups (ground and EDT), subsequent treatments of chromium plating, electroless NiP coating and plasma nitriding were carried out. The results of the reciprocating tests showed that specimens with electroless NiP coating presented the lowest friction coefficients, while plasma nitrided specimens showed the highest. In general, previous surface texturing before the coating/surface modification increased the wear of the counter bodies. Oneexceptionwas for EDT with subsequent electroless NiP coating, which presented the lowest counter bodies wear rate. The samples withelectroless NiP coating promoted a tribolayer consisting of Nickel, Phosphorus and Oxygen on both the specimens andthecounter bodies, which was apparently responsible for the reduction of friction coefficient and wear rate. The increase of the test time reduced the wear rate of the samples, apparently due the stability of the tribolayers formed, except for the nitrided samples. For the textured specimens, NiP coating showed the best performance in maintaining the surface topography of the specimens after the sliding tests.

Estudio comparativo de cinco métodos para determinar ciertas constantes físicas del suelo

En el presente trabajo, se estudió la comparación de cinco diferentes métodos aplicados en la determinación de la capacidad de campo en porcentaje de humedad,coeficiente de Marchitez en porcentaje de humedad, Peso volumetrico en gramos por centímetro cubico, la calibración del método para la determinación de la capacidad de campo, se considero el procedimiento mas adecuado para determinar el volumen de agua en metros cúbicos que hay que agregar a un suelo, para ser llevado a su capacidad de campo, el porcentaje de humedad critica, y el numero de días que tarda un suelo al pasar de su capacidad de campo a su coeficiente de Marchitez. Se usaron muestras de diferentes suelos, pertenecientes a las series Esquipulas, Sabana Grande, Nejapa y Majada; se usaron los métodos del Tamiz, Bureta y Bomba de vacío para la determinación de la capacidad de campo, el método del tomate para la determinación del coeficiente de Marchitez y los métodos de la Parafina y el cilindro, para la determinación del peso volumetrico. Se considero para la determinación de la capacidad de campo en porcentaje de humedad, el promedio deducido de un numero de cinco pruebas realizadas al emplear el método del tamiz, y el promedio deducido de un numero de diez pruebas hechas, utilizando los métodos de la Bureta y de la Bomba de vacío respectivamente. similarmente, se considero para la determinación del coeficiente de Marchitez, el promedio resultante de la repetición de dos veces la misma prueba en cada suelo. En la determinación del peso volumetrico en g/cc., se considero igualmente, el promedio obtenido de cinco pruebas hechas en los suelos de las series de Esquipulas, Nejapa y Majada utilizando el método de la parafina y el promedio obtenido de siete pruebas realizadas en el suelo de las serie de Sabana Grande usando 4 cilindros de 500 cc., 2 cilindros de 150 cc y un cilindro de 100 cc., empleando en esta prueba consecuentemente el método del cilindro. Para la determinación del volumen de agua en metros cubicos, se considero la utilización de los promedios de la capacidad de campo, coeficiente de Marchitez y peso volumetrico. Se empleo para este calculo la formula Va= (CC-CM)xPV x Area x profundidad, 100 , en donde (Va)corresponde al volumen de agua, (CC) a la capacidad de campo, (CM) al coeficiente de marchitez, (PV) al peso volumetrico, (Area) a la superficie en metros cuadrados a que se tomaron las muestras y (profundidad) corresponde a la profundidad a que se tomaron las muestras de suelo. Para la determinación del porcentaje de humedad critica, se considero los datos promedios de capacidad de campo y coeficiente de marchitez, así como el limite critico de 85% considerado como constante. Se realizo análisis estadístico de los métodos usados para cada suelo, se calculo la regresión de los porcentajes de humedad sobre los días transcurridos para alcanzar la marchitez permanente, se calculo la ecuación de predicción y la significación del coeficiente de regresión. El método de la bomba de vacío fue el menos variable de los métodos usados en la determinación de la capacidad de campo y suele ser el mas indicado para el calculo del volumen de agua y el porcentaje de humedad critica. Las características texturales y estructurales de los suelos estudiados fue determinante en la variabilidad de los métodos usados. Se concluyo diciendo que toda serie de suelo que presente las características texturales y estructurales de las series sometidas a estas determinaciones, pueden ser consideradas con valores similares a los valores de cada una de las constantes obtenidas y que sus posibilidades de riego, estarán directamente relacionadas a los promedios de los valores encontrados.

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.

Influência de propriedades físico químicas dos materiais resinosos e da técnica de inserção na adaptação marginal de restaurações classe II

A contração de polimerização das resinas compostas é uma característica indesejável que compromete a integridade da interface dente/restauração. O objetivo deste estudo foi avaliar in vitro a influência de diferentes materiais usados em restaurações classe II de resina composta, quanto ao grau de conversão, tensão de contração, resistência a flexão, módulo de elasticidade e formação de fenda marginal. Foram realizados preparos classe II com dimensões de 4x4x2mm em terceiros molares recém-extraídos para a avaliação da formação de fenda marginal. As cavidades foram niveladas com cimento de ionômero de vidro Riva Light Cure (SDI) (CIV), resina de baixa contração SureFilSDR (Dentsply) (SDR), resina flow FiltekZ350Flow (3M/ESPE) (Z350F) e resina composta FiltekP90 (3M/ESPE) (P90). As restaurações (n=3) foram avaliadas com lupa estereoscópica. A resistência a flexão foi avaliada por meio de ensaio de flexão em três pontos. Para este ensaio foram confeccionados dez corpos de prova (n=10) de cada material com dimensões de 10x2x1mm. Para o teste de tensão de contração foram utilizados cilindros de polimetacrilato com 5 mm de diâmetro e 13 ou 28mm de comprimento. Os bastões foram fixados na EMIC com um espaço de 2mm entre eles, onde os materiais foram inseridos. Foram realizadas cinco repetições para cada grupo (n=5) e a tensão proveniente da contração foi medida por até 10 minutos após o início da fotopolimerização. O Grau de Conversão (GC) foi determinado por espectroscopia no infravermelho com transformada de Fourier (FTIR). Os resultados foram tratados estatisticamente por análise de variância (ANOVA) e Teste de Tukey (p<0,05). Fenda marginal: Z350F = CIV > SDR = P90. Tensão de contração: Z350F > SDR > CIV = P90. Resistência a flexão: P90 > SDR = Z350F > CIV. Módulo de Elasticidade: P90 > CIV = SDR = Z350F. GC: Z350F = SDR > P90 > CIV. Conclusões: existe correlação entre a formação de fenda marginal e as propriedades físico químicas dos materiais testados, sendo as resinas de baixa contração que proporcionaram melhor adaptação marginal; existe correlação entre resistência a flexão, módulo de elasticidade, tensão de contração e a composição dos materiais, já que os compósitos com melhores resultados foram os que apresentaram os maiores percentuais de carga, no entanto, maior grau de conversão não representou melhores propriedades mecânicas.

Emissão de CO2 do solo e sua correlação com a rizosfera de diferentes paisagens de áreas mineradas do município de Santo Antônio de Pádua-RJ

Objetivando avaliar o comportamento das emissões de CO2 do solo em áreas mineradas do município de Santo Antônio de Pádua-RJ e sua correlação com a rizosfera, este presente estudo utilizou uma câmara fechada com sensor de infravermelho em três diferentes paisagens, a saber: A-1 (área reflorestada há 10 anos), A-2 (área desmatada) e A-3 (área em processo de recuperação). Em cada área foi instalada três cilindros para efeitos de repetição. O monitoramento foi realizado durante os meses representativos de cada estação do ano de 2013, sendo a análise realizada durante dois dias consecutivos. Concomitantemente as coletas de CO2 foram realizadas coletas de dados de temperatura e umidade do solo, sendo também avaliadas informações pedológicas através das análises de granulometria, porosidade, pH, carbono orgânico e matéria orgânica. Informações meteorológicas e microclimatológicas também foram extraídas através de uma estação meteorológica automática e através de sensores portáteis. Os resultados permitem concluir que existe uma variação sazonal dos fluxos de CO2, havendo uma tendência de máximos de emissão durante o verão e de mínimas durante o inverno, sendo o outono e a primavera marcados por valores medianos. A correlação das áreas entre os dois dias monitoramento indicam que as emissões foram semelhantes ao da análise em dia anterior, apresentando uma correlação significativa a 5% para A-1 e A-2 e de 1% para A-3. A-1 e A-2 apresentaram emissões de CO2 mais homogêneas que A-3, havendo, entretanto, um maior fluxo de CO2 durante o verão para todas as áreas. Os dados de MOS, COS e pH demonstraram não haver uma correlação direta com as emissões de CO2. Os dados de porosidade e densidade, porém, apontam para uma possível correlação com as menores emissões de CO2 em A-3 devido a menor porosidade e maior densidade de seus solos. A temperatura do solo foi a variável que mais se correlacionou com as emissões de CO2, havendo um índice igual a r =0,68 para A-1 e de r =0,74 para A-2, sendo que em A-3 esta correlação não foi significativa. A temperatura do ar demonstrou uma correlação somente na área descampada de A-2. No que se refere à correlação da umidade do solo não houve correlações diretas significativas, sendo que somente houve uma correlação negativa (r=-0,50) significativa a 5% em A-3 com a umidade do ar. O diagnóstico ambiental das áreas de monitoramento revela que estas possuem baixos indicadores de qualidade, sendo afetados também pela escassez hídrica da região durante oito meses do ano. A-1 apresenta os melhores indicadores biológicos, químicos e microclimáticos, seguidos por A-2 e A-3 que apresentam diversas deficiências e problemas em termos de estrutura e atividade biológica dos solos. Neste estudo permite-se concluir que áreas próximas, porém com características distintas podem produzir diferentes padrões de emissão de CO2, dificultando, portanto, estimativas globais de emissão de CO2. Os elementos mais associados às emissões de CO2 parecem estar relacionados à temperatura do solo e do ar, umidade do ar e estrutura do solo, havendo, entretanto, outros fatores que podem estar indiretamente relacionados e que exercem diferentes influências de acordo com o ambiente analisado.

Avaliação do grau de porosidade de três cimentos endodônticos: estudo realizado com microtomogafia computadorizada e análise digital de imagens

O presente trabalho teve como objetivo avaliar volumetricamente a presença de poros em três cimentos obturadores. Para a análise de porosidade, quatro cilindros de cada cimento foram preparados e escaneados usando um microtomógrafo de alta resolução (Skyscam 1174, Kontich, Bélgica). O cálculo da porosidade foi realizado por meio de análise de imagens digitalizadas dos blocos de cimentos. Os quais foram microtomografados para criação de modelos tridimensionais. A presença de poros e vacúolos foi então avaliada por inferência do software CT analiser. Os resultados mostraram que o i-Root SP teve o menor índice de porosidade (0,07%), enquanto o AH plus e o MTA Fillapex não apresentaram diferenças estatisticamente significativas entre si (p≥0,05). Apesar dos resultados para o índice de porosidade total do MTA Fillapex e do AH plus não terem diferenças significativas(p>0,05), os achados do presente trabalho mostraram que o MTA fillapex obteve resultados significativamente maiores nos volumes médios individuais dos poros internos que o Ah plus e o i-Root SP. Os resultados foram tabulados e analisados estatisticamete através do teste Anova ao nível de significância de 5%.

Medición de la capacidad de nitrificación mediante la técnica de incubaciones in situ en suelos cultivados con maíz

p.101-114

Análise probabilística de segurança de barragens gravidade de betão

Trabalho Final de Mestrado para obtenção do grau de Mestre em Engenharia Civil na Área de Especialização de Estruturas

Metrología dimensional.

En el libro se desarrollan 16 capítulos: Unidades, Errores, Causas de error, Equipos de medida, Patrones, Normalización de ajustes, Medida de redondez, Control del acabado superficial, Mediciones de longitud, Medidas por comparación, Medida de ángulos, Medida de conos y radios de cilindros y esferas, Planitud y rectitud, Verificación de engranajes, Verificación de roscas, y Verificación de las máquinas herramientas. Al finalizar el último capítulo se ofrece un vocabulario de los términos metrológicos más significativos, relacionados con los temas de: magnitudes y unidades, mediciones, resultados de medición, instrumentos de medida, características de los instrumentos de medida y patrones.