A importância clínica da vitamina D

Projeto de Pós-Graduação/Dissertação apresentado à Universidade Fernando Pessoa como parte dos requisitos para obtenção do grau de Mestre em Ciências Farmacêuticas

Thermal analysis of LEDS for liquid crystal display's backlighting

This paper investigated the thermal design of the light emitting diode (LED)onto the board and its packaging. The LED was a 6-lead MultiLED with three chips designed for LCD backlighting and other lighting purposes. A 3D finite element model of this LED was built up and thermal analysis was carried out using the multi physics software package PHYSICA. The modeling results were presented as temperature distributions in each LED, and the predicted junction temperature was used for thermal resistance calculation. The results for the board structure indicated that (1) removing the foil attach decreased the thermal resistance, (2) Increasing the copper foil thickness reduced the thermal resistance. package design indicated that the SMT designed LED with integrated slug gave lower thermal resistance. Pb-free solder material gave lower thermal resistance and junction temperature when compared with conductive adhesive

Gas-liquid two phase flow through a vertical 90deg elbow bend

Pressure drop data are reported for two phase air-water flow through a vertical to horizontal 90° elbow bend set in 0.026 m i.d. pipe. The pressure drop in the vertical inlet tangent showed some significant differences to that found for straight vertical pipe. This was caused by the elbow bend partially choking the inflow resulting in a build-up of pressure and liquid in the vertical inlet riser and differences in the structure of the flow regimes when compared to the straight vertical pipe. The horizontal outlet tangent by contrast gave data in general agreement with literature even to exhibiting a drag reduction region at low liquid rates and gas velocities between 1 and 2 m s -1. The elbow bend pressure drop was best correlated in terms of le/d determined using the actual pressure loss in the inlet vertical riser. The data showed a general increase with fluid rates that tapered off at high fluid rates and exhibited a negative pressure region at low rates. The latter was attributed to the flow being smoothly accommodated by the bend when it passed from slug flow in the riser to smooth stratified flow in the outlet tangent. A general correlation was presented for the elbow bend pressure drop in terms of total Reynolds numbers. A modified Lockhart-Martinelli model gave prediction of the data.

A Universal Flow Regime Map for Horizontal Two-Phase Flow in Pipes

A new universal flow map has been developed for two-phase co-current flow. The map has been successfully tested against wide variety of data. Flow regime transition predictors suggested by other authors have been shown to be useful. New transitional models are proposed for the stratified to annular regimes, blow through slug and intermittent regimes.

Self-potential signatures associated with an injection experiment at an in situ biological permeable reactive barrier

Strategies available to evaluate the performance of in situ permeable reactive barriers are currently not well developed and often rely on fluid and media sampling directly from the permeable reactive barrier (PRB). Here, we investigate the utility of the self-potential (SP) method as a technique to monitor in situ PRB performance. Our field study was conducted at in situ biological PRB in Portadown, Northern Ireland, UK, which was emplaced to assist in the remediation of groundwater contamination (e.g., hydrocarbons, ammonia) that resulted from the operations and waste disposal practices of a former gasworks. Borehole SP measurements were collected during the injection of contaminant groundwater slugs in an attempt to monitor/detect the response of the microbial activity associated with the breakdown of the added contaminants into the PRB. In addition, an uncontaminated groundwater slug was injected into a different portion of the PRB as a ‘control’ and SP measurements were collected for comparison to the SP response of the contaminant slugs. The results of the SP signals due to the contaminant injections show that the magnitude of the response was relatively small (<10 mV) yet showed a consistent decrease during both contaminant injections. The net decrease in SP recorded during the contaminant injections slowly rebounded to near background values through ~44 hours post-injection. The SP response during the uncontaminated injection showed a slight, albeit negligible (within the margin of error), 1 mV increase in the measured SP signals, in contrast to the contaminant injections. The results of the SP signals recorded from the uncontaminated groundwater injection also persisted through a period of ~47 hours after injection but show a net increase in SP relative to pre-injection values. Based on the difference in SP response between the contaminated and uncontaminated injections, we suggest that the responses are likely to be the result of differences in the chemistry of the injection types (contaminated versus uncontaminated) and in situ groundwater. We argue that the SP signals associated with the contaminated injections are dominated by diffusion (electrochemical) potential, possibly enhanced by a microbial effect. While the results of our investigation show a consistent SP response associated with the contaminant injections that is dominated by diffusional effects, further studies are required in order to better understand the effect of microbial activity on SP signals and the potential utility for the SP method to detect/monitor changes that may be indicative of biological PRB performance.

Phase-Transfer Catalysis in Segmented Flow in a Microchannel: Fluidic Control of Selectivity and Productivity

Precise control over the interfacial area of aqueous and organic slugs in segmented flow in a microchannel reactor provides an attractive means to optimize the yield and productivity of a phase-transfer-catalyzed reaction. Herein, we report the selective alkylation of phenylacetonitrile to the monoalkylated product in a microchannel of 250-mu m internal diameter operated in a continuous and solvent-free manner in the slug-flow regime. The conversion of phenylacetonitrile increased from 40% to 99% as a result of a 97% larger slug surface-to-volume ratio when the volumetric aqueous-to-organic phase flow ratio was raised from 1.0 to 6.1 at the same residence time. The larger surface-to-volume ratio significantly promoted catalyst phase transfer but decreased selectivity because of the simultaneous increase of the rate of the consecutive reaction to the dialkylated product. There exists all Optimum flow ratio with a maximum productivity. Conversion and selectivity in the microchannel reactor were both found to be significantly larger than in a stirred reactor.

Non-aqueous silicone elastomer gels as a vaginal microbicide delivery system for the HIV-1 entry inhibitor maraviroc

Aqueous semi-solid polymeric gels, such as those based on hydroxyethylcellulose (HEC) and polyacrylic acid (e.g. Carbopol®), have a long history of use in vaginal drug delivery. However, despite their ubiquity, they often provide sub-optimal clinical performance, due to poor mucosal retention and limited solubility for poorly water-soluble actives. These issues are particularly pertinent for vaginal HIV microbicides, since many lead candidates are poorly water-soluble and where a major goal is the development of a coitally independent, once daily gel product. In this study, we report the use of a non-aqueous silicone elastomer gel for vaginal delivery of the HIV-1 entry inhibitor maraviroc. In vitro rheological, syringeability and retention studies demonstrated enhanced performance for silicone gels compared with a conventional aqueous HEC gel, while testing of the gels in the slug model confirmed a lack of mucosal irritancy. Pharmacokinetic studies following single dose vaginal administration of a maraviroc silicone gel in rhesus macaques showed higher and sustained MVC levels in vaginal fluid, vaginal tissue and plasma compared with a HEC gel containing the same maraviroc loading. The results demonstrate that non-aqueous silicone gels have potential as a formulation platform for coitally independent vaginal HIV microbicides.

Pressure drop of gas–liquid Taylor flow in round micro-capillaries for low to intermediate Reynolds numbers

In this paper, a model is presented that describes the pressure drop of gas-liquid Taylor flow in round capillaries with a channel diameter typically less than 1 mm. The analysis of Bretherton (J Fluid Mech 10:166-188, 1961) for the pressure drop over a single gas bubble for vanishing liquid film thickness is extended to include a non-negligible liquid film thickness using the analysis of Aussillous and Qu,r, (Phys Fluids 12(10):2367-2371, 2000). This result is combined with the Hagen-Poiseuille equation for liquid flow using a mass balance-based Taylor flow model previously developed by the authors (Warnier et al. in Chem Eng J 135S:S153-S158, 2007). The model presented in this paper includes the effect of the liquid slug length on the pressure drop similar to the model of Kreutzer et al. (AIChE J 51(9):2428-2440, 2005). Additionally, the gas bubble velocity is taken into account, thereby increasing the accuracy of the pressure drop predictions compared to those of the model of Kreutzer et al. Experimental data were obtained for nitrogen-water Taylor flow in a round glass channel with an inner diameter of 250 mu m. The capillary number Ca (gl) varied between 2.3 x 10(-3) and 8.8 x 10(-3) and the Reynolds number Re (gl) varied between 41 and 159. The presented model describes the experimental results with an accuracy of +/- 4% of the measured values.

Liquid-Liquid Flow in a Capillary Microreactor: Hydrodynamic Flow Patterns and Extraction Performance

The capillary micro reactor, with four stable operating flow patterns and a throughput range from grams per hour to kilograms per hour, presents an attractive alternative to chip-based and microstructured reactors for laboratory- and pilot-scale applications. In this article, results for the extraction of 2-butanol from toluene under different flow patterns in a water/toluene flow in long capillary microreactors are presented. The effects of the capillary length (0.4-2.2 m), flow rate (0.1-12 mL/min), and aqueous-to-organic volumetric flow ratio (0.25-9) on the slug, bubbly, parallel, and annular flow hydrodynamics were investigated. Weber-number-dependent flow maps were composed for capillary lengths of 0.4 and 2 m that were used to interpret the flow pattern formation in terms of surface tension and inertia forces. When the capillary length was decreased from 2 to 0.4 m, a transition from annular to parallel flow was observed. The capillary length had little influence on slug and bubbly flows. The flow patterns were evaluated in terms of stability, surface-to-volume ratio, throughput, and extraction efficiency. Slug and bubbly flow operations yielded 100% thermodynamic extraction efficiency, and increasing the aqueous-to-organic volumetric ratio to 9 allowed for 99% 2-butanol extraction. The parallel and annular flow operating windows were limited by the capillary length, thus yielding maximum 2-butanol extractions of 30% and 47% for parallel and annular flows, respectively.

Hydrodynamics and mixer-induced bubble formation in micro bubble columns with single and multiple-channels

A hydrodynamic characterization of an industrially used gas-liquid contacting microchannel. device is discussed, viz. the micro bubble column of IMM. Furthermore, similar characterization of a gas-liquid flow microchip of TU/e, with two tailored mixer designs, is used to solve fundamental issues on hydrodynamics, and therefore, to achieve further design and operating optimization of that chip and the IMM device. Flow pattern maps are presented in a dimensionless fashion for further predictions on new fluidic systems for optimum single-channel multiphase operation. Bubble formation was investigated in the two types of mixers and pinch-off and hydrodynamic decay mechanisms are observed. The impact of these mechanisms on bubble size, bubble size distributions, and on the corresponding flow patterns, i.e., the type of mixer design, can be decisive for the flow pattern map and thus, may be used to alter flow pattern maps. The bubble sizes and their distribution were improved for the tailored designs, i.e., smaller and more regular bubbles were generated. Finally, the impact of multi-channel distribution for gas and liquid flow is demonstrated. Intermediate flow patterns such as slug-annular flow, also found for single-phase operation, and the simultaneous coexistence of flow regimes are presented, with the latter providing evidence of flow maldistribution.

Indirect-drive inertial confinement fusion using highly supersonic, radiatively cooled, plasma slugs

We present a new approach to indirect-drive inertial confinement fusion which makes use of highly supersonic, radiatively cooled, slugs of plasma to energize a hohlraum. 2D resistive magnetohydrodynamic simulations of slug formation in shaped liner Z -pinch implosions are presented along with 2D-radiation-hydrodynamic simulations of the slug impacting a converter foil and 3D-view-factor simulations of a double-ended hohlraum. Results for the Z facility at Sandia National Laboratory indicate that two synchronous slugs of 250 kJ kinetic energy could be produced, resulting in a capsule surface temperature of similar to225 eV .

Numbered-up gas-liquid micro/milli channels reactor with modular flow distributor

Gas-liquid processing in microreactors remains mostly restricted to the laboratory scale due to the complexity and expenditure needed for an adequate numbering-up with a uniform flow distribution. Here, the numbering-up is presented for multi-phase (gas-liquid) flow in microreactor suitable for a production capacity of kg/h. Based on the barrier channels concept, the barrier-based micro/milli reactor (BMMR) is designed and fabricated to deliver flow non-uniformity of less than 10%. The BMMR consists of eight parallel channels all operated in the Taylor flow regime and with a liquid flow rate up to 150. mL/min. The quality of the flow distribution is reported by studying two aspects. The first aspect is the influence of different viscosities, surface tensions and flow rates. The second aspect is the influence of modularity by testing three different reaction channels type: (1) square channels fabricated in a stainless steel plate, (2) square channels fabricated in a glass plate, and (3) circular channels (capillaries) made of stainless steel. Additionally, the BMMR is compared to that of a single channel regard the slug and bubble lengths and bubble generation frequency. The results pave the ground for bringing multi-phase flow in microreactor one step closer for large scale production via numbering-up. © 2012 Elsevier B.V.

Mutant p53 expression in fallopian tube epithelium drives cell migration

Ovarian cancer is the fifth leading cause of cancer death among US women. Evidence supports the hypothesis that high-grade serous ovarian cancers (HGSC) may originate in the distal end of the fallopian tube. Although a heterogeneous disease, 96% of HGSC contain mutations in p53. In addition, the "p53 signature," or overexpression of p53 protein (usually associated with mutation), is a potential precursor lesion of fallopian tube derived HGSC suggesting an essential role for p53 mutation in early serous tumorigenesis. To further clarify p53-mutation dependent effects on cells, murine oviductal epithelial cells (MOE) were stably transfected with a construct encoding for the R273H DNA binding domain mutation in p53, the most common mutation in HGSC. Mutation in p53 was not sufficient to transform MOE cells but did significantly increase cell migration. A similar p53 mutation in murine ovarian surface epithelium (MOSE), another potential progenitor cell for serous cancer, was not sufficient to transform the cells nor change migration suggesting tissue specific effects of p53 mutation. Microarray data confirmed expression changes of pro-migratory genes in p53(R273H) MOE compared to parental cells, which could be reversed by suppressing Slug expression. Combining p53(R273H) with KRAS(G12V) activation caused transformation of MOE into high-grade sarcomatoid carcinoma when xenografted into nude mice. Elucidating the specific role of p53(R273H) in the fallopian tube will improve understanding of changes at the earliest stage of transformation. This information can help develop chemopreventative strategies to prevent the accumulation of additional mutations and reverse progression of the "p53 signature" thereby, improving survival rates.

Tecnologia vinagreira: desenvolvimento de novos produtos vinagreiros na ESAS

O vinagre é obtido por dupla fermentação alcoólica e acética de substâncias de origem agrícola, possuindo cada tipo um flavour particular, função dos substratos e tecnologia usados, mantendo gosto sui generis ácido. A sua aptidão tecnológica viabiliza o fabrico de múltiplos produtos, macerando especiarias, plantas, etc, conduzindo ao enriquecimento da matriz, cujo perfil químico ganha complexidade e novas características sensoriais/funcionais. A picklagem fresh pack é um processo alternativo de conservação em vinagre, sem fermentação. Com vinagres de fermentação submergida, desenvolveram-se na ESAS (2009-2013), dois vinagres e um vinagrete com adições e um pickles de frutos doces, articulando ensaios tecnológicos, laboratoriais e sensoriais. Concebidos como produtos gourmet, pretendeu-se oferecer inovação e conveniência. Além do longo tempo de vida de prateleira, evidencia-se: 1) no vinagre de vinho branco com mirtilo –a mais-valia de preservar o fruto inteiro, por efeito de picklagem; 2) no vinagre agridoce, de vinho tinto Touriga Nacional com mel e especiarias –uma tónica agridoce equilibrada e actual; 3) no vinagrete de laranja aromatizado –a complexidade aromática aliada à sensação de frescura na boca; 4) no pickles fresh pack de pera-abacaxi agridoce –novidade e dupla utilização: consumida a fruta, a infusão utiliza-se como vinagre de mesa (aptidão incomum em pickles).---Vinegar is obtained by double fermentation alcoholic and acetic of substances from agricultural origin, each type having one particular flavor, due to the technology and the substrates used, while maintaining sui generis acid taste. Its technological aptitude enables the manufacture of multiple products, macerating spices, plants, leading to the enrichment of the matrix whose chemical profile becomes increasingly complex with new sensory/functional characteristics. The fresh pack process is an alternative process of pickling, without fermentation. With submerged fermentation vinegar, two vinegars and a vinaigrette with additions and pickled sweet fruits were developed in ESAS (2009-2013), articulating technological, laboratory and sensory tests. Designed as gourmet products, intended to provide innovation and convenience. In addition to the long shelf life, stands out: 1) in white wine vinegar with blueberries – the added value of preserving the whole fruit by pickling effect, 2) in bittersweet red wine vinegar, Touriga Nacional with honey and spices – the sweet and sour taste, balanced and fashionable; 3) in flavored orange vinaigrette – the aromatic complexity coupled with the fresh sensation in the mouth, 4) in the fresh pack sweet and sour pickles with pear-pineapple – the innovation and dual-use: consumed the fruit, infusion is used as table vinegar (unusual application for pickles).

Reciclagem termoquímica de resíduos de plásticos e de pneus por pirólise

A sociedade moderna encontra-se cada vez mais dependente dos combustíveis líquidos bem como de produtos derivados do petróleo. Em virtude do limitado tempo de vida das reservas naturais de petróleo, torna-se imperativo encontrar fontes alternativas de produção de hidrocarbonetos. A pirólise de resíduos de pneus e plásticos pode ser uma dessas possíveis fontes. Neste processo, o tratamento termoquímico implementado aos resíduos permite, não só, a valorização económica resultante da sua transformação em produtos de valor acrescido, como também a recuperação do conteúdo orgânico. O referido processo conduz à formação de hidrocarbonetos em fase líquida que podem ser utilizados pela indústria como combustíveis líquidos e/ou como matéria-prima. O presente trabalho tem como objectivo principal a definição das condições experimentais mais propícias à obtenção de combustíveis líquidos (maximização) resultantes da pirólise de misturas de resíduos de borracha de pneus e plásticos nomeadamente polietileno (PE), polipropileno (PP) e poliestireno (PS). Como instrumento de optimização das condições experimentais optou-se pela Metodologia dos Planos Factoriais de Ensaios. Os resultados experimentais obtidos mostram que as taxas de conversão em fase líquida podem atingir valores superiores a 80% (m/m) dependendo das condições experimentais utilizadas bem como do tipo e mistura de resíduos a pirolisar. Os rendimentos das fracções gasosa e sólida podem atingir valores na ordem dos 5% e 12% (respectivamente). Foi também estudado o efeito das condições experimentais nomeadamente a temperatura de reacção, pressão inicial, tempo de reacção e composição da mistura. Este estudo revelou que a maximização da fracção líquida é favorecida por uma temperatura de ensaio de 370ºC, uma pressão inicial de 0,48MPa e um tempo de ensaio de 15 minutos. Relativamente à composição da mistura, os melhores resultados foram obtidos com 30% (m/m) de resíduos de borracha de pneus (BP) associados a uma mistura de 70% (m/m) de resíduos de plásticos composta por 20% polietileno, 30% polipropileno e 20% poliestireno. Igualmente foi feita a caracterização física e química da matéria-prima e dos produtos obtidos pelo referido processo, bem como, o estudo da presença de diferentes substâncias potencialmente doadores de hidrogénio ao meio reaccional de forma a melhorar o rendimento líquido. Por último, foram realizados estudos cinéticos das reacções químicas de formação dos diferentes produtos aos resíduos de borracha de pneus (BP), misturas de resíduos de plástico (PE, PP e PS) e suas misturas. Ainda, foram ajustados os resultados obtidos pelo modelo teórico aos resultados experimentais, propostos mecanismos reaccionais de formação dos produtos e calculados os parâmetros cinéticos. De acordo com os resultados obtidos, a pirólise pode representar um papel significativo na valorização energética e orgânica destes resíduos apesar de, ainda, ser necessário o desenvolvimento de alguns aspectos tecnológicos de modo a tornar mais atraente a implementação desta tecnologia à escala industrial.