Síntese e caracterização de esferas monodispersas de látex e sua utilização no preparo de filmes de cristais coloidais tridimensionais

Esferas de poliestireno foram obtidas através da polimerização do estireno sem a presença de emulsificante. A suspensão foi caracterizada por Espalhamento de Luz e Microscopia Eletrônica de Transmissão apresentando monodispersidade com tamanho em torno de 463 nm. O método de deposição vertical foi utilizado para preparar filmes em substratos de vidro a partir da suspensão de esferas. Filmes de opalas de alta qualidade foram obtidos e caracterizados por Espectroscopia de Reflectância, Microscopia Eletrônica de Varredura e Microscopia Óptica.

Uutto-olosuhteiden vaikutus kasviperäisen indigon saantoon

Indigo on väriaine, jota valmistetaan petrokemianteollisuuden välituotteena syntyvästä aniliinista. Indigolla on kuitenkin pitkä historia. Sitä on valmistettu perinteisesti eri viljelykasveista, joista Euroopassa merkittävin on ollut morsinko. Luonnonmukaisten tuotteiden suosion kasvaessa on ryhdytty selvittämään morsingon viljelyn potentiaalia. Viljelyn kannattavuuden kannalta olennaista on kasvin lehdissä esiintyvien indigon esiasteiden mahdollisimman täydellinen eristäminen. Indigoa tuotetaan uuttamalla indigon esiasteet veteen. Esiasteet hajoavat synnyttäen indoksyyliä, josta hapen vaikutuksella muodostuu indigoa. Syntynyt indigo saostuu ja laskeutuu pohjalle. Samalla kuitenkin tapahtuu epätoivottuja sivureaktioita, jotka vähentävät indigon saantoa. Tutkimuksen tavoitteena oli laboratorio- ja kenttäkokeiden avulla löytää indigon saantoa parantavat uutto-olosuhteet. Kokeiden perusteella havaittiin, että indigon saantoon vaikuttavat positiivisesti pH:n laskeminen, lämpötilan nostaminen, morsingon lehtien pilkkominen ja uuttoliuoksen sekoittaminen. Uuttoliuoksen suolapitoisuuden havaittiin puolestaan vaikuttavan indigon saantoon negatiivisesti. Laboratoriokokeiden perusteella havaittu pH:n laskemisen vaikutus indigon saantoon todistettiin myös kenttäolosuhteissa. Kokeiden havaintojen perusteella esitettiin olosuhteiden indigosaantoa parantavien vaikutusten johtuvan kahdesta tekijästä: indoksyylin stabiloitumisesta happamassa ympäristössä, jolloin sivureaktioiden osuus vähenee, sekä aineensiirron paranemisella sekoituksen, faasien rajapinnan kasvamisen ja etenkin lehtien vahakerroksen rikkoutumisen kuuman veden ja hapon vaikutuksesta.

Características físico-químicas de ácidos húmicos em diferentes etapas da vermicompostagem

Amostras de materiais coletados em diferentes estádios de vermicompostagem foram submetidas a procedimentos de extração de ácidos húmicos. Técnicas de titulação potenciométrica, termogravimetria (DTG), difração de raios X e espectrofotometria no uv/visível e no infravermelho foram utilizadas no estudo desses materiais. Os dados de titulação foram submetidos ao ajuste por regressão não-linear, determinando-se, assim, cinco valores de pKa característicos de cinco classes de grupos tituláveis. Nas curvas DTG, foram observadas duas etapas, sendo a primeira característica da separação de estruturas alifáticas e, ou, alicíclicas e a segunda, a decomposição de estruturas aromáticas. A difratometria de raios X apresentou diferenças marcantes nos resultados, principalmente nos três primeiros picos onde parecem ocorrer reorganização estrutural e polimerização ao longo do processo de vermicompostagem. Os espectros do infravermelho não apresentaram diferenciação entre os espectros. Os valores da razão E4/E6 encontrados estão de acordo com os característicos dos ácidos húmicos, mas não fornecem informações que possam contribuir para a elucidação da estrutura e formação desses ácidos.

Improving the calculation of rate of stratification in APROS

APROS (Advanced Process Simulation Environment) is a computer simulation program developed to simulate thermal hydraulic processes in nuclear and conventional power plants. Earlier research at VTT Technological Research Centre of Finland had found the current version of APROS to produce inaccurate simulation results for a certain case of loop seal clearing. The objective of this Master’s thesis is to find and implement an alternative method for calculating the rate of stratification in APROS, which was found to be the reason for the inaccuracies. Brief literature study was performed and a promising candidate for the new method was found. The new method was implemented into APROS and tested against experiments and simulations from two test facilities and the current version of APROS. Simulation results with the new version were partially conflicting; in some cases the new method was more accurate than the current version, in some the current method was better. Overall, the new method can be assessed as an improvement.

Parâmetros cinéticos de adesivos produzidos a partir de taninos de Anadenanthera peregrina e Eucalyptus grandis

Devido à crise do petróleo, na década de 70, pesquisas tiveram o objetivo de substituir parcial ou totalmente os adesivos convencionais, à base de petróleo. Uma forma de substituição foi a utilização de fontes naturais, como os taninos, provenientes de algumas espécies arbóreas. Porém, os taninos apresentam algumas limitações de uso, que podem ser superadas através da sulfitação e da hidrolise ácida. Portanto, o objetivo deste trabalho foi avaliar o efeito da hidrólise ácida e sulfitação de taninos extraídos da casca de Eucalyptus grandis e Anadenanthera peregrina, nos parâmetros cinéticos dos adesivos tânicos, através da técnica de calorimetria diferencial exploratória (DSC). Os taninos foram hidrolisados com ácido acético ou ácido clorídrico a 10N, empregando-se três valores de pH e três tempos de reação. A sulfitação foi realizada em solução de sulfito de sódio, à 5%, em três tempos de reação. A energia de ativação, entalpia e temperatura de cura dos adesivos foram reduzidas pela hidrólise e sulfitação dos taninos, porém apresentaram banda larga de polimerização. O tempo de reação dos taninos não teve efeito sobre os parâmetros cinéticos.

Kytkentäaineet puumuovikomposiiteissa

Puumuovikomposiittien valmistuksessa yhdistetään kaksi toisistaan eroavaa materiaalia jolloin saadaan aikaan materiaalien ominaisuuksien ainutlaatuinen yhdistelmä. Polymeerimateriaaleina käytetään pääasiassa erilaisia kestomuoveja. Kuitumateriaaleina voidaan käyttää puujauhetta, sahanpurua, paperin- ja kartongin valmistuksessa käytettävää sellua, nanoselluloosaa tai muita puukuitumateriaaleja. Polaarisen puukuidun ja polaarittoman muovimateriaalin välinen materiaalien rajapinnan adheesio on yleensä riittämätöntä, mikä vaikuttaa lopputuotteen ominaisuuksien heikkenemiseen. Kyseinen ongelma on pyritty ratkaisemaan käyttämällä erilaisia kytkentäaineita. Tässä työssä keskitytään käsittelemään erilaisia puumuovikomposiittien kytkentäaineita, niiden toimintaa sekä vaikutuksia lopputuotteeseen. Lisäksi työssä esitellään myös puumuovikomposiittien valmistusmateriaaleja ja valmistusprosesseja.

Model-based estimation of liquid flows in the blast furnace hearth and taphole

This thesis presents a set of methods and models for estimation of iron and slag flows in the blast furnace hearth and taphole. The main focus was put on predicting taphole flow patterns and estimating the effects of various taphole conditions on the drainage behavior of the blast furnace hearth. All models were based on a general understanding of the typical tap cycle of an industrial blast furnace. Some of the models were evaluated on short-term process data from the reference furnace. A computational fluid dynamics (CFD) model was built and applied to simulate the complicated hearth flows and thus to predict the regions of the hearth exerted to erosion under various operating conditions. Key boundary variables of the CFD model were provided by a simplified drainage model based on the first principles. By examining the evolutions of liquid outflow rates measured from the furnace studied, the drainage model was improved to include the effects of taphole diameter and length. The estimated slag delays showed good agreement with the observed ones. The liquid flows in the taphole were further studied using two different models and the results of both models indicated that it is more likely that separated flow of iron and slag occurs in the taphole when the liquid outflow rates are comparable during tapping. The drainage process was simulated with an integrated model based on an overall balance analysis: The high in-furnace overpressure can compensate for the resistances induced by the liquid flows in the hearth and through the taphole. Finally, a recently developed multiphase CFD model including interfacial forces between immiscible liquids was developed and both the actual iron-slag system and a water-oil system in laboratory scale were simulated. The model was demonstrated to be a useful tool for simulating hearth flows for gaining understanding of the complex phenomena in the drainage of the blast furnace.

Detection of Horizontal Two-Phase Flow Patterns Through a Neural Network Model

One of the main problems related to the transport and manipulation of multiphase fluids concerns the existence of characteristic flow patterns and its strong influence on important operation parameters. A good example of this occurs in gas-liquid chemical reactors in which maximum efficiencies can be achieved by maintaining a finely dispersed bubbly flow to maximize the total interfacial area. Thus, the ability to automatically detect flow patterns is of crucial importance, especially for the adequate operation of multiphase systems. This work describes the application of a neural model to process the signals delivered by a direct imaging probe to produce a diagnostic of the corresponding flow pattern. The neural model is constituted of six independent neural modules, each of which trained to detect one of the main horizontal flow patterns, and a last winner-take-all layer responsible for resolving when two or more patterns are simultaneously detected. Experimental signals representing different bubbly, intermittent, annular and stratified flow patterns were used to validate the neural model.

Development of a process for the direct synthesis of hydrogen peroxide in a novel microstructured reactor

Microreactors have proven to be versatile tools for process intensification. Over recent decades, they have increasingly been used for product and process development in chemical industries. Enhanced heat and mass transfer in the reactors due to the extremely high surfacearea- to-volume ratio and interfacial area allow chemical processes to be operated at extreme conditions. Safety is improved by the small holdup volume of the reactors and effective control of pressure and temperature. Hydrogen peroxide is a powerful green oxidant that is used in a wide range of industries. Reduction and auto-oxidation of anthraquinones is currently the main process for hydrogen peroxide production. Direct synthesis is a green alternative and has potential for on-site production. However, there are two limitations: safety concerns because of the explosive gas mixture produced and low selectivity of the process. The aim of this thesis was to develop a process for direct synthesis of hydrogen peroxide utilizing microreactor technology. Experimental and numerical approaches were applied for development of the microreactor. Development of a novel microreactor was commenced by studying the hydrodynamics and mass transfer in prototype microreactor plates. The prototypes were designed and fabricated with the assistance of CFD modeling to optimize the shape and size of the microstructure. Empirical correlations for the mass transfer coefficient were derived. The pressure drop in micro T-mixers was investigated experimentally and numerically. Correlations describing the friction factor for different flow regimes were developed and predicted values were in good agreement with experimental results. Experimental studies were conducted to develop a highly active and selective catalyst with a proper form for the microreactor. Pd catalysts supported on activated carbon cloths were prepared by different treatments during the catalyst preparation. A variety of characterization methods were used for catalyst investigation. The surface chemistry of the support and the oxidation state of the metallic phase in the catalyst play important roles in catalyst activity and selectivity for the direct synthesis. The direct synthesis of hydrogen peroxide was investigated in a bench-scale continuous process using the novel microreactor developed. The microreactor was fabricated based on the hydrodynamic and mass transfer studies and provided a high interfacial area and high mass transfer coefficient. The catalysts were prepared under optimum treatment conditions. The direct synthesis was conducted at various conditions. The thesis represents a step towards a commercially viable direct synthesis. The focus is on the two main challenges: mitigating the safety problem by utilization of microprocess technology and improving the selectivity by catalyst development.

Computational studies for the design of process equipment with complex geometries

This study combines several projects related to the flows in vessels with complex shapes representing different chemical apparata. Three major cases were studied. The first one is a two-phase plate reactor with a complex structure of intersecting micro channels engraved on one plate which is covered by another plain plate. The second case is a tubular microreactor, consisting of two subcases. The first subcase is a multi-channel two-component commercial micromixer (slit interdigital) used to mix two liquid reagents before they enter the reactor. The second subcase is a micro-tube, where the distribution of the heat generated by the reaction was studied. The third case is a conventionally packed column. However, flow, reactions or mass transfer were not modeled. Instead, the research focused on how to describe mathematically the realistic geometry of the column packing, which is rather random and can not be created using conventional computeraided design or engineering (CAD/CAE) methods. Several modeling approaches were used to describe the performance of the processes in the considered vessels. Computational fluid dynamics (CFD) was used to describe the details of the flow in the plate microreactor and micromixer. A space-averaged mass transfer model based on Fick’s law was used to describe the exchange of the species through the gas-liquid interface in the microreactor. This model utilized data, namely the values of the interfacial area, obtained by the corresponding CFD model. A common heat transfer model was used to find the heat distribution in the micro-tube. To generate the column packing, an additional multibody dynamic model was implemented. Auxiliary simulation was carried out to determine the position and orientation of every packing element in the column. This data was then exported into a CAD system to generate desirable geometry, which could further be used for CFD simulations. The results demonstrated that the CFD model of the microreactor could predict the flow pattern well enough and agreed with experiments. The mass transfer model allowed to estimate the mass transfer coefficient. Modeling for the second case showed that the flow in the micromixer and the heat transfer in the tube could be excluded from the larger model which describes the chemical kinetics in the reactor. Results of the third case demonstrated that the auxiliary simulation could successfully generate complex random packing not only for the column but also for other similar cases.

Membrane properties of structurally modified ceramides : effects on lipid lateral distribution and sphingomyelin-interactions in artificial bilayer membranes

Ceramides comprise a class of sphingolipids that exist only in small amounts in cellular membranes, but which have been associated with important roles in cellular signaling processes. The influences that ceramides have on the physical properties of bilayer membranes reach from altered thermodynamical behavior to significant impacts on the molecular order and lateral distribution of membrane lipids. Along with the idea that the membrane physical state could influence the physiological state of a cell, the membrane properties of ceramides have gained increasing interest. Therefore, membrane phenomena related to ceramides have become a subject of intense study both in cellular as well as in artificial membranes. Artificial bilayers, the so called model membranes, are substantially simpler in terms of contents and spatio-temporal variation than actual cellular membranes, and can be used to give detailed information about the properties of individual lipid species in different environments. This thesis focuses on investigating how the different parts of the ceramide molecule, i.e., the N-linked acyl chain, the long-chain sphingoid base and the membrane-water interface region, govern the interactions and lateral distribution of these lipids in bilayer membranes. With the emphasis on ceramide/sphingomyelin(SM)-interactions, the relevance of the size of the SMhead group for the interaction was also studied. Ceramides with methylbranched N-linked acyl chains, varying length sphingoid bases, or methylated 2N (amide-nitrogen) and 3O (C3-hydroxyl) at the interface region, as well as SMs with decreased head group size, were synthesized and their bilayer properties studied by calorimetric and fluorescence spectroscopic techniques. In brief, the results showed that the packing of the ceramide acyl chains was more sensitive to methyl-branching in the mid part than in the distal end of the N-linked chain, and that disrupting the interfacial structure at the amide-nitrogen, as opposed to the C3-hydroxyl, had greater effect on the interlipid interactions of ceramides. Interestingly, it appeared that the bilayer properties of ceramides could be more sensitive to small alterations in the length of the long-chain base than what was previously reported for the N-linked acyl chain. Furthermore, the data indicated that the SM-head group does not strongly influence the interactions between SMs and ceramides. The results in this thesis illustrate the pivotal role of some essential parts of the ceramide molecules in determining their bilayer properties. The thesis provides increased understanding of the molecular aspects of ceramides that possibly affect their functions in biological membranes, and could relate to distinct effects on cell physiology.

Reducing contact resistance in graphene devices

In this thesis, the contact resistance of graphene devices was investigated because high contact resistance is detrimental to the performance of graphene field-effect transistors (GFET). Method for increasing so-called edge-contact area was applied in device fabrication process, as few nanometers thick Ni layer was used as a catalytic etchant during the annealing process. Finally, Ni was also used as a metal for contact. GFETs were fabricated using electron beam lithography using graphene fabricated by chemical vapor deposition (CVD). Critical part of the fabrication process was to preserve the high quality of the graphene channel while etching the graphene at contact areas with Ni during the annealing. This was achieved by optimizing the combination of temperature and gas flows. The structural properties of graphene were studied using scanning electron microscopy, scanning confocal μ-Raman spectroscopy and optical microscopy. Evaluation of electric transport properties including contact resistance was carried out by transmission line method and four-probe method. The lowest contact resistance found was about at 350 Ωμm. In addition, different methods to transfer CVD graphene synthesized on copper were studied. Typical method using PMMA as a supporting layer leaves some residues after its removal, thus effecting on the performance of a graphene devices. In a metal assisted transfer method, metal is used as an interfacial layer between PMMA and graphene. This allows more effective removal of PMMA. However, Raman spectra of graphene transferred by metal assisted method showed somewhat lower quality than the PMMA assisted method

Liberação e atividade de moléculas indutoras de fitoalexinas em rubiáceas tropicais: influência da metilesterificação de pectinas

Duas espécies arbóreas tropicais de Rubiaceae, Alibertia myrcifolia e Rudgea jasminoides, diferem na composição de pectinas de suas paredes celulares e na capacidade de produzir fitoalexinas quando inoculadas com fungos. Essas espécies foram comparadas em relação ao mecanismo de liberação e atividade de oligossacarídeos de paredes celulares indutores da síntese de fitoalexinas. Paredes celulares das espécies hidrolisadas com Driselase, por diferentes períodos, mostraram que oligossacarídeos indutores podem ser liberados a partir de paredes de ambas espécies, embora sejam mais facilmente obtidos de R. jasminoides, espécie que apresenta capacidade de sintetizar fitoalexinas. A incubação das paredes celulares com endopoligalacturonase promoveu a liberação de oligossacarídeos de R. jasminoides, mas não de A. myrcifolia, espécie que não produz fitoalexinas. A hidrólise seqüencial com pectinametilesterase e endopoligalacturonase, que promoveu a quebra da parece celular e a liberação de moléculas eliciadoras a partir de A. myrcifolia, indicou a presença de pectinas com diferente grau de metilesterificação entre as espécies analisadas. Adicionalmente, oligossacarídeos com pequeno grau de polimerização mostraram atividade inibidora da síntese de fitoalexinas induzidas por um eliciador fúngico e por oligossacarídeos com maior grau de polimerização. Esses resultados sugerem que a diferença no comportamento das duas rubiáceas com relação à indução de fitoalexinas em soja possa estar relacionada ao mecanismo de liberação de oligossacarídeos, como conseqüência das diferenças no grau de metilesterificação e distribuição dos grupos metil-ésteres das pectinas.

Catalytic direct synthesis of hydrogen peroxide in a novel microstructured reactor

The direct synthesis from hydrogen and oxygen is a green alternative for production of hydrogen peroxide. However, this process suffers from two challenges. Firstly, mixtures of hydrogen and oxygen are explosive over a wide range of concentrations (4-94% H2 in O2). Secondly, the catalytic reaction of hydrogen and oxygen involves several reaction pathways, many of them resulting in water production and therfore decreasing selectivity. The present work deals with these two challenges. The safety problem was dealed by employing a novel microstructured reactor. Selectivity of the reaction was highly improved by development a set of new catalysts. The final goal was to develop an effective and safe continuous process for direct synthesis of hydrogen peroxide from H2 and O2. Activated carbon cloth and Sibunit were examined as the catalysts’ supports. Palladium and gold monometallic and palladium-gold bimetallic catalysts were thoroughly investigated by numerous kinetic experiments performed in a tailored batch reactor and several catalyst charachterization methods. A complete set of data for direct synthesis of H2O2 and its catalytic decomposition and hydrogenation was obtained. These data were used to assess factors influencing selectivity and activity of the catalysts in direct synthesis of H2O2 as well as its decomposition and hydrogenation. A novel microstructured reactor was developed based on hydrodynamics and mass transfer studies in prototype microstractural plates. The shape and the size of the structural elements in the microreactor plate were optimized in a way to get high gas-liquid interfacial area and gas-liquid mass transfer. Finally, empirical correlations for the volumetric mass transfer coefficient were derived. A bench-scale continuous process was developed by using the novel microstructral plate reactor. A series of kinetic experiments were performed to investigate the effects of the gas and the liquid feed rates and their ratio, the amount of the catalyst, the gas feed composition and pressure on the final rate of H2O2 production and selectivity.

COMPORTAMENTO DO ÓLEO DE GIRASSOL COM ALTO TEOR DE ÁCIDO OLÉICO EM TERMOXIDAÇÃO E FRITURA

Óleos de sementes de girassol com diferentes níveis de ácido oléico foram utilizados sob condições de termoxidação e fritura para avaliar o comportamento do óleo de girassol com alto teor de ácido oléico quanto ao seu grau de insaturação quando comparado com o óleo de girassol convencional. Os métodos analíticos aplicados incluíram a determinação de compostos polares totais, quantificação de compostos glicerídicos menores, quantificação da composição triglicerídica, período de indução a 100oC e níveis de a -tocoferol. Os resultados para compostos polares totais apresentaram menores valores em óleo de girassol com alto teor de ácido oléico quando comparados com óleo de girassol convencional. Quanto à distribuição dos compostos glicerídicos menores, verificou-se, de modo geral, que o aumento dos compostos polares totais estava relacionado essencialmente aos compostos de maior peso molecular, isto é, polímeros, dímeros e triglicerídios oxidados, os quais são representantes das alterações térmica e oxidativa. Já os diglicerídios e ácidos graxos, indicativos da alteração hidrolítica, permaneceram praticamente nos níveis originais; uma vez que a umidade não se encontrava presente no meio. A perda quantitativa da composição triglicerídica dependeu do grau de insaturação do triglicerídio, sendo mais elevada em triglicerídios que contêm duas ou três moléculas de ácido linoléico. Em todos os casos, o óleo de girassol convencional teve uma maior tendência à polimerização, um maior grau de alteração total e uma maior perda de triglicerídios majoritários que o óleo de girassol com alto teor de ácido oléico. Assim, dentre os óleos utilizados neste estudo, os resultados mostraram um excelente comportamento do óleo de girassol com alto teor de ácido oléico em relação à termoxidação, independente do tipo de aquecimento e à fritura descontínua. Tais resultados demonstraram que sua resistência à alteração termoxidativa estava relacionada com seu baixo teor em ácidos graxos polinsaturados e alto teor em ácido oléico e trioleína.