Determination of minimum fluidization velocity for gas-solid beds by experimental data and numerical simulations

The purpose of this work is to predict the minimum fluidization velocity Umf in a gas-solid fluidized bed. The study was carried out with an experimental apparatus for sand particles with diameters between 310μm and 590μm, and density of 2,590kg/m3. The experimental results were compared with numerical simulations developed in MFIX (Multiphase Flow with Interphase eXchange) open source code [1], for three different sizes of particles: 310mum, 450μm and 590μm. A homogeneous mixture with the three kinds of particles was also studied. The influence of the particle diameter was presented and discussed. The Ergun equation was also used to describe the minimum fluidization velocity. The experimental data presented a good agreement with Ergun equation and numerical simulations. Copyright © 2011 by ASME.

Multiphase Screen Development

This honors thesis research project was the study and development of a compact separation device for the oil and gas industry involving a multiphase cylindrical screen filter. Cylindrical screens can be used for solids removal in multiphase flow in upstream oil and gas applications. This study focused on cylindrical wire-wrap screen test unit design and performance characterization to determine volumetric flow rate and pressure drop correlations. The project goals were met with research, test unit design, CFD modeling, calculations, and physical testing. The comprehensive testing will take place during the summer of 2013 and is planned to consist of building the designed flowloop and housing and using high capacity pumps to achieve higher flow rates. Multiphase testing will be performed with water, air, and sand particles and flow and pressure effects will be evaluated for solids filtering over time.

Microbial community, biomarker concentrations and their isotopic signature in sediment of Gullfaks and Tommeliten methane seeps in the Northern North Sea

Gullfaks is one of the four major Norwegian oil and gas fields, located in the northeastern edge of the North Sea Plateau. Tommeliten lies in the greater Ekofisk area in the central North Sea. During the cruises HE 208 and AL 267 several seep locations of the North Sea were visited. At the Heincke seep at Gullfaks, sediments were sampled in May 2004 (HE 208) using a video-guided multiple corer system (MUC; Octopus, Kiel). The samples were recovered from an area densely covered with bacterial mats where gas ebullition was observed. The coarse sands limited MUC penetration depth to maximal 30 centimeters and the highly permeable sands did not allow for a high-resolution, vertical subsampling because of pore water loss. The gas flare mapping and videographic observation at Tommeliten indicated an area of gas emission with a few small patches of bacterial mats with diameters <50 cm from most of which a single stream of gas bubbles emerged. The patches were spaced apart by 10-100 m. Sampling of sediments covered by bacterial mats was only possible with 3 small push cores (3.8 cm diameter) mounted to ROV Cherokee. These cores were sampled in 3 cm intervals. Lipid biomarker extraction from 10 -17 g wet sediment was carried out as described in detail elsewhere (Elvert et al., 2003; doi:10.1080/01490450303894). Briefly, defined concentrations of cholestane, nonadecanol and nonadecanolic acid with known delta 13C-values were added to the sediments prior to extraction as internal standards for the hydrocarbon, alcohol and fatty acid fraction, respectively. Total lipid extracts were obtained from the sediment by ultrasonification with organic solvents of decreasing polarity. Esterified fatty acids (FAs) were cleaved from the glycerol head group by saponification with methanolic KOH solution. From this mixture, the neutral fraction was extracted with hexane. After subsequent acidification, FAs were extracted with hexane. For analysis, FAs were methylated using BF3 in methanol yielding fatty acid methyl esters (FAMES). The fixation for total cell counts and CARD-FISH were performed on-board directly after sampling. For both methods, sediments were fixed in formaldehyde solution. After two hours, aliquots for CARD-FISH staining were washed with 1* PBS (10mmol/l sodium phosphate solution, 130mmol/l NaCl, adjusted to a pH of 7.2) and finally stored in a 1:1 PBS:ethanol solution at -20°C until further processing. Samples for total cell counts were stored in formalin at 4°C until analysis. For sandy samples, the total cell count/CARD-FISH protocol was optimized to separate sand particles from the cells. Cells were dislodged from sediment grains and brought into solution with the supernatant by sonicating each sample onice for 2 minutes at 50W. This procedure was repeated four times and supernatants were combined. The sediment samples were brought to a final dilution of 1:2000 to 1:4000 and filtered onto 0.2µm GTTP filters (Millipore, Eschbonn, Germany).

Gasificação de biomassa num reator de leito fluidizado à escala piloto

A gasificação de biomassa permite a produção de um gás combustível com capacidade para reduzir o consumo de combustíveis fósseis. Contudo, para promover a utilização deste processo a nível industrial é necessário ultrapassar diversas limitações e elaborar tecnologias de gasificação que sejam mais rentáveis e eficientes. No presente trabalho efetuou-se a gasificação direta com ar, num reator auto-térmico com um leito fluidizado borbulhante, de diferentes tipos de biomassa provenientes da floresta portuguesa, nomeadamente pellets de madeira e diferentes tipos de biomassa florestal residual derivada de eucalipto. A investigação foi realizada numa instalação à escala piloto localizada no Departamento de Ambiente e Ordenamento da Universidade de Aveiro. A infraestrutura foi desenvolvida de modo a permitir o estudo do processo de gasificação de biomassa. O reator utilizado apresenta 3 metros de altura, consistindo a câmara de gasificação em 2.25 metros, 0.25 metros de diâmetro interno e uma potência entre 40 e 70 kWth. O leito é composto por areia (partículas com granulometria entre os 355 e 1000 µm) e tem uma altura de 0.23 m. A infraestrutura experimental oferece condições para efetuar a gasificação de biomassa, determinar a composição do gás produzido em termos de CO, CO2, H2, N2, CH4 e C2H4 e efetuar a sua combustão num queimador localizado a jusante do reator. O leito fluidizado operou com temperaturas médias entre os 700 e 850ºC. Para as razões de equivalência estabelecidas, entre 0.17 e 0.36, o gás seco apresentou uma composição que, em termos volumétricos e em função das condições operatórias, variou entre 14.0 a 21.4% CO, 14.2 a 17.5% CO2, 3.6 a 5.8% CH4, 1.3 a 2.4% C2H4, 2.0 a 10.2% H2 e 48.9 a 61.1% N2. A maior concentração de CO, CH4 e C2H4 foi observada durante a gasificação de biomassa residual florestal derivada de eucalipto com razão de equivalência de 0.17, contudo, a maior concentração de H2 foi obtida na gasificação de pellets de madeira com razão de equivalência de 0.25. Tendo em conta a composição gasosa, o poder calorífico inferior do gás seco encontrou-se entre 4.4 e 6.9 MJ/Nm3 e os valores mais elevados foram observados durante os processos de gasificação efetuados com menor razão de equivalência. A produção específica de gás variou entre 1.2 e 2.2 Nm3/kg biomassa bs, a eficiência do gás arrefecido entre 41.1 e 62.6% e a eficiência de conversão de carbono entre 60.0 e 87.5%, encontrando-se na gama dos valores reportados na literatura. A melhor condição, em termos da eficiência de gás arrefecido, consistiu na gasificação de biomassa residual florestal derivada de eucalipto com razão de equivalência de 0.25, e em termos da produção específica de gás seco e eficiência de conversão de carbono, na gasificação de biomassa residual florestal derivada de eucalipto com razão de equivalência de 0.35. Contudo, o gás com maior poder calorífico inferior foi obtido durante a gasificação de biomassa residual florestal derivada de eucalipto com razão de equivalência de 0.17. O reator demonstrou adequabilidade na gasificação de diferentes tipos de biomassa e foram observadas condições estáveis de operação, tanto em termos de temperatura como da composição do gás produzido. Geralmente, o gás apresentou propriedades combustíveis apropriadas para ser comburido de forma contínua e estável pelo queimador de gás, sem ser necessária uma fonte de ignição permanente ou a utilização de um combustível auxiliar.

Adsorção de cromo (VI) em leito fixo utilizando partículas de areia recobertas com Quitosana

Neste trabalho foi avaliado o processo de recobrimento de partículas de areia com quitosana utilizando a técnica dip-coating, e analisado o emprego destas partículas como recheio de uma coluna de leito fixo no processo de adsorção de cromo (VI) em solução aquosa. A quitosana foi obtida a partir de resíduos de camarão e caracterizada. O estudo avaliou a influência do tamanho das partículas e da concentração da solução de quitosana no recobrimento das partículas de areia. Foram avaliados parâmetros termodinâmicos, isotermas de equilíbrio e parâmetros relacionados ao funcionamento do leito (vazão e pH da solução, diâmetro de partícula) para o processo de adsorção de cromo (VI) em solução aquosa. No recobrimento das partículas de areia, o tamanho não teve significância na resposta, enquanto a concentração da solução de recobrimento mostrou ter grande influência sobre o resultado, sendo que a menor concentração de quitosana dentro da faixa estudada (0,5% p/v) apresentou o melhor desempenho. O processo de cura física para o recobrimento das partículas de areia mostrou melhor desempenho para a adsorção de cromo (VI) em leito fixo frente ao processo físico-químico. As análises de superfície (MEV) e de difração de raio-X (EDX) comprovaram a mudança na superfície das partículas recobertas e a presença de cromo após a adsorção. O modelo de Sips foi o que melhor representou os dados experimentais de equilíbrio, com R2 >0,99% e EMR<3,5%, sendo que a capacidade máxima de adsorção foi de 46,93 mg g-1 obtida a 298 K. O processo se mostrou espontâneo, exotérmico e favorável, com valores de -4,49 a -4,66kJ mol-1 para e energia livre de Gibbs, -5,97kJ mol-1 para a variação de entalpia e -5,17x10-3 kJ mol-1K -1 para variação de entropia. O aumento do pH diminuiu a adsorção de cromo (VI), sendo que a melhor resposta foi obtida em pH 3, sendo que o diâmetro de partícula não teve efeito significante. O estudo da vazão da solução de cromo (VI) no desempenho do leito mostrou que no menor valor (2,5 mL min-1 ) a concentração de saída do leito foi próxima a zero, mantendo-se com concentrações de saída abaixo de 20% por pelo menos 20 min. O estudo da dessorção do leito mostrou que após cinco ciclos de trabalho o leito manteve 86% da capacidade de adsorção, com taxas de recuperação do cromo no processo de dessorção maiores que 95%.

Panel prefabricado a base de fibras naturales

En este trabajo de investigación, se diseñó y desarrollo un panel prefabricado para aplicaciones arquitectónicas, compuesto por fibras naturales. El panel fue elaborado a partir de una mezcla de fibras vegetales de tamo de arroz y cabuya, con partículas de arena silícea, los cuales, están aglomerados con una resina de silicato de sodio. La mezcla de estos materiales tiene buenas propiedades de trabajabilidad, compactación y con la aplicación de dióxido de carbono CO2, esta mezcla se solidifica rápidamente. Esta técnica, facilita el proceso de producción en serie de los paneles prefabricados de fibras naturales. A través del moldeo con una prensa manual, se obtuvo paneles con buenas propiedades y características de resistencia, módulo de ruptura, densidad y contenido de humedad; además de tener medidas modulares, texturas de agradable aspecto superficial y criterios de reversibilidad. Los paneles también presentan favorables cualidades de aislamiento térmico y acústico. Sus aplicaciones y utilidades son para revestimiento en espacios interiores de: muros, cielo raso y tabiquería liviana o decorativa. Finalmente se generó una propuesta de instalación de los paneles, utilizando de igual forma recursos renovables y sostenibles.

Stream power criterion and design of sand bed channels at incipient motion

The critical stream power criterion may be used to describe the incipient motion of cohesionless particles of plane sediment beds. The governing equation relating ``critical stream power'' to ``shear Reynolds number'' is developed by using the present experimental data as well as the data from several other sources. Simultaneously, a resistance equation, relating the ``particle Reynolds number'' to the``shear Reynolds number'' is developed for plane sediment beds in wide channels with little or no transport. By making use of these relations, a procedure is developed to design plane sediment beds such that any two of the four design variables, including particle size, energy/friction slope, flow depth, and discharge per unit width in the channel should be known to predict the remaining two variables. Finally, a straightforward design procedure using design tables/design curves and analytical methods is presented to solve six possible design problems.

Measurement of resistivity and dielectric constant of beach-sand minerals

Resistivity and dielectric constant are important parameters which influence the separation of particles in a drum-type electrostatic separator. The paper provides details of the measurement of the parameters and data on the magnitude of resistivity and dielectric constant of the minerals of beach sand.

Oxide Particle Surface Chemistry and Ion Transport in "Soggy Sand" Electrolytes

The crucial role of oxide surface chemical composition on ion transport in "soggy sand" electrolytes is discussed in a systematic manner. A prototype soggy sand electrolytic system comprising aerosil silica functionalized with various hydrophilic and hydrophobic moieties dispersed in lithium perchlorate-ethylene glycol solution was used for the study. Detailed rheology studies show that the attractive particle network in the case of the composite with unmodified aerosil silica (with surface silanol groups) is most favorable for percolation in ionic conductivity, as well as rendering the composite with beneficial elastic mechanical properties: Though weaker in strength compared to the composite with unmodified aerosil particles, attractive particle networks are also observed in composites of aerosil particles with surfaces partially substituted with hydrophobic groups. The percolation in ionic conductivity is, however, dependent on the size of the hydrophobic moiety. No spanning attractive particle network was formed for aerosil particles with surfaces modified with stronger hydrophilic groups (than silanol), and as a result, no percolation in ionic conductivity was observed. The composite with hydrophilic particles was a sol, contrary to gels obtained in the case of unmodified aerosil, and partially substituted with hydrophobic groups.

Design of plane sand-bed channels affected by seepage

The importance of seepage in the design of channels is discussed. Experimental investigations reveal that seepage, either in the downward direction (suction) or in the upward direction (injection), can significantly change the resistance as well as the mobility of the sand-bed particles. A resistance equation relating 'particle Reynolds number' and 'shear Reynolds number' under seepage conditions is developed for plane sediment beds. Finally, a detailed design procedure of the plane sediment beds affected by seepage is presented.

Influence of Oxide Particle Network Morphology on Ion Solvation and Transport in ``Soggy Sand''Electrolytes

The role of oxide surface chemical composition and solvent on ion solvation and ion transport of ``soggy sand'' electrolytes are discussed here. A ``soggy sand'' electrolyte system comprising dispersions of hydrophilic/hydrophobic functionalized aerosil silica in lithium perchlorate methoxy polyethylene glycol solution was employed for the study. Static and dynamic rheology measurements show formation of an attractive particle network in the case of the composite with unmodified aerosil silica (i.e., with surface silanol groups) as well as composites with hydrophobic alkane groups. While particle network in the composite with hydrophilic aerosil silica (unmodified) were due to hydrogen bonding, hydrophobic aerosil silica particles were held together via van der Waals forces. The network strength in the latter case (i.e., for hydrophobic composites) were weaker compared with the composite with unmodified aerosil silica. Both unmodified silica as well as hydrophobic silica composites displayed solid-like mechanical strength. No enhancement in ionic conductivity compared to the liquid electrolyte was observed in the case of the unmodified silica. This was attributed to the existence of a very strong particle network, which led to the ``expulsion'' of all conducting entities from the interfacial region between adjacent particles. The ionic conductivity for composites with hydrophobic aerosil particles displayed ionic conductivity dependent on the size of the hydrophobic chemical moiety. No spanning attractive particle network was observed for aerosil particles with surfaces modified with stronger hydrophilic groups (than silanol). The composite resembled a sol, and no percolation in ionic conductivity was observed.

Incipient motion design of sand bed channels affected by bed suction

Seepage through sand bed channels in a downward direction (suction) reduces the stability of particles and initiates the sand movement. Incipient motion of sand bed channel with seepage cannot be designed by using the conventional approach. Metamodeling techniques, which employ a non-linear pattern analysis between input and output parameters and solely based on the experimental observations, can be used to model such phenomena. Traditional approach to find non-dimensional parameters has not been used in the present work. Parameters, which can influence the incipient motion with seepage, have been identified and non-dimensionalized in the present work. Non-dimensional stream power concept has been used to describe the process. By using these non-dimensional parameters; present work describes a radial basis function (RBF) metamodel for prediction of incipient motion condition affected by seepage. The coefficient of determination, R-2 of the model is 0.99. Thus, it can be said that model predicts the phenomena very well. With the help of the metamodel, design curves have been presented for designing the sand bed channel when it is affected by seepage. (C) 2010 Elsevier B.V. All rights reserved.