865 resultados para heating stage
Resumo:
The development of a malaria vaccine seems to be a definite possibility despite the fact that even individuals with a life time of endemic exposure do not develop sterile immunity. An effective malaria vaccine would be invaluable in preventing malaria-associated deaths in endemic areas, especially amongst children less than 5 years of age and pregnant women. This review discusses our current understanding of immunity against the asexual blood stage of malaria - the stage that is responsible for the symptoms of the disease - and approaches to the design of an asexual blood stage vaccine.
Resumo:
Merozoite surface protein 1 (MSP1) of malaria parasites undergoes proteolytic processing at least twice before invasion into a new RBC. The 42-kDa fragment, a product of primary processing, is cleaved by proteolytic enzymes giving rise to MSP1(33), which is shed from the merozoite surface, and MSP1(19), which is the only fragment carried into a new RBC. In this study, we have identified T cell epitopes on MSP1(33) of Plasmodium yoelii and have examined their function in immunity to blood stage malaria. Peptides 20 aa in length, spanning the length of MSP1(33) and overlapping each other by 10 aa, were analyzed for their ability to induce T cell proliferation in immunized BALB/c and C57BL/6 mice. Multiple epitopes were recognized by these two strains of mice. Effector functions of the dominant epitopes were then investigated. Peptides Cm15 and Cm21 were of particular interest as they were able to induce effector T cells capable of delaying growth of lethal P. yoelii YM following adoptive transfer into immuno-deficient mice without inducing detectable Ab responses. Homologs of these epitopes could be candidates for inclusion in a subunit vaccine.
Resumo:
The effect of heating and cooling on heart rate in the estuarine crocodile Crocodylus porosus was studied in response to different heat transfer mechanisms and heat loads. Three heating treatments were investigated. C. porosus were: (1) exposed to a radiant heat source under dry conditions; (2) heated via radiant energy while half-submerged in flowing water at 23degreesC and (3) heated via convective transfer by increasing water temperature from 23degreesC to 35degreesC. Cooling was achieved in all treatments by removing the heat source and with C. porosus half-submerged in flowing water at 23degreesC. In all treatments, the heart rate of C. porosus increased markedly in response to heating and decreased rapidly with the removal of the heat source. Heart rate during heating was significantly faster than during cooling at any given body temperature, i.e. there was a significant heart rate hysteresis. There were two identifiable responses to heating and cooling. During the initial stages of applying or removing the heat source, there was a dramatic increase or decrease in heart rate ('rapid response'), respectively, indicating a possible cardiac reflex. This rapid change in heart rate with only a small change or no change in body temperature (
Resumo:
Adiabatic self-heating tests were carried out on five New Zealand coal samples ranging in rank from lignite to high-volatile bituminous. Kinetic parameters of oxidation were obtained front the self-heating curves assuming Arrhenius behaviour. The activation energy E (kJ mol(-1)) and the pre-exponential factor A (s(-1)) were determined in the temperature range of 70-140 degreesC. The activation energy exhibited a definite rank relationship with a minimum E of 55 kJ mol(-1) occurring at a Suggate rank of similar to6.2 corresponding to subbituminous C. Either side of this rank there was a noticeable increase in the activation energy indicating lower reactivity of the coal. A similar rank trend was also observed in the R-70 self-heating rate index values that were taken from the initial portion of the self-heating curve front 40 to 70 degreesC. From these results it is clear that the adiabatic method is capable of providing reliable kinetic parameters of coal oxidation.
Resumo:
We evaluated patients with end-stage heart failure who have a high likelihood of response to cardiac resynchronization therapy (biventricular pacing). It appears that 20% of patients do not respond to this expensive therapy despite the use of selection criteria (dilated cardiomyopathy, heart failure, New York Heart Association class II or IV, left ventricular election fraction 120 ms). The presence of left ventricular dys-synchrony is needed to result in improvement after cardiac resynchronization therapy. (C)2003 by Excerpta Medica, Inc.
Resumo:
Background. The purpose of this study was to examine the reliability of stage of change (SOC) measures for moderate-intensity and vigorous physical activity in two separate samples of young adults. Staging measures have focused on vigorous exercise, but current public health guidelines emphasize moderate-intensity activity. Method. For college students in the USA (n = 105) and in Australia (n = 123), SOC was assessed separately on two occasions for moderate-intensity activity and for vigorous activity. Test-retest repeatability was determined, using Cohen's kappa coefficient. Results. In both samples, the reliability scores for the moderate-intensity physical activity staging measure were lower than the scores for the vigorous exercise staging measure. Weighted kappa values for the moderate-intensity staging measure were in the fair to good range for both studies (0.50 and 0.45); for the vigorous staging measure kappa values were excellent and fair to good (0.76 and 0.72). Conclusions. There is a need to standardize and improve methods for staging moderate-intensity activity, given that such measures are used in public health interventions targeting HEPA (health-enhancing physical activity). (C) 2003 American Health Foundation and Elsevier Science (USA). All rights reserved.
Resumo:
Improvement of the environmental performance of processes and products is a common objective in industry, and has been receiving increased attention in recent years. The main objective of this work is to evaluate the potential environmental impact of two bedding products, a polyurethane foam mattress (PFM) and a pocket spring mattress (PSM). These two types are the most common mattresses used in Europe. A Life Cycle Assessment (LCA) shows that the PFM has a higher environmental impact than the PSM. For both products the main cause of environmental impact is the manufacturing process, respectively the polyurethane foam block moulding process for the PFM, and the pocket spring nucleus process for the PSM. A scenario analysis shows the possibility of reducing the environmental impact of the products’ life cycle using an alternative End-of-Life scenario, resorting to incineration rather than landfill. Two strategies were also studied in order to reduce the environmental impact of the PFM: (1) reutilization of foam that was sent to the waste system management, and (2) a 20% weight reduction of the polyurethane foam. The second strategy has proven to be the most effective.
Resumo:
Only three cases of human infection by anisakid nematodes have been reported in Chile since 1976. In the present case, an anisakid worm, identified as a fourth-stage Pseudoterranova decipiens larva, was removed with a gastroendoscopic biopsy clipper from the stomach of a 45 year-old man from southern Chile. The patient, who presented acute epigastric pain and a continuous sensation of having an empty stomach, reported having eaten smoked fish. The worm was fixed in 70% ethanol and cleaned in lactophenol for morphological study. The morphometric characteristics of the worm are described and drawn. Anisakid larvae in fish flesh can be killed by freezing or cooking.
Resumo:
New K/Ar dating and geochemical analyses have been carried out on the WNW-ESE elongated oceanic island of S. Jorge to reconstruct the volcanic evolution of a linear ridge developed close to the Azores triple junction. We show that S. Jorge sub-aerial construction encompasses the last 1.3 Myr, a time interval far much longer than previously reported. The early development of the ridge involved a sub-aerial building phase exposed in the southeast end of the island and now constrained between 1.32 +/- 0.02 and 1.21 +/- 0.02 Ma. Basic lavas from this older stage are alkaline and enriched in incompatible elements, reflecting partial melting of an enriched mantle source. At least three differentiation cycles from alkaline basalts to mugearites are documented within this stage. The successive episodes of magma rising, storage and evolution suggest an intermittent reopening of the magma feeding system, possibly due to recurrent tensional or trans-tensional tectonic events. Present data show a gap in sub-aerial volcanism before a second main ongoing building phase starting at about 750 ka. Sub-aerial construction of the S. Jorge ridge migrated progressively towards the west, but involved several overlapping volcanic episodes constrained along the main WNW-ESE structural axis of the island. Malic magmas erupted during the second phase have been also generated by partial melting of an enriched mantle source. Trace element data suggest, however, variable and lower degrees of partial melting of a shallower mantle domain, which is interpreted as an increasing control of lithospheric deformation on the genesis and extraction of primitive melts during the last 750 kyr. The multi-stage development of the S. Jorge volcanic ridge over the last 1.3 Myr has most likely been greatly influenced by regional tectonics, controlled by deformation along the diffuse boundary between the Nubian and the Eurasian plates, and the increasing effect of sea-floor spreading at the Mid-Atlantic Ridge.
Resumo:
A Blumlein line is a particular Pulse Forming Line, PFL, configuration that allows the generation of high-voltage sub-microsecond square pulses, with the same voltage amplitude as the dc charging voltage, into a matching load. By stacking n Blumlein lines one can multiply in theory by n the input dc voltage charging amplitude. In order to understand the operating behavior of this electromagnetic system and to further optimize its operation it is fundamental to theoretically model it, that is to calculate the voltage amplitudes at each circuit point and the time instant that happens. In order to do this, one needs to define the reflection and transmission coefficients where impedance discontinuity occurs. The experimental results of a fast solid-state switch, which discharges a three stage Blumlein stack, will be compared with theoretical ones.
Resumo:
Characteristics of tunable wavelength filters based on a-SiC:H multi-layered stacked cells are studied both theoretically and experimentally. Results show that the light-activated photonic device combines the demultiplexing operation with the simultaneous photodetection and self amplification of an optical signal. The sensor is a bias wavelength current-controlled device that make use of changes in the wavelength of the background to control the power delivered to the load, acting a photonic active filter. Its gain depends on the background wavelength that controls the electrical field profile across the device.
Resumo:
MOR zeolites were modified via desilication treatments with NaOH, under conventional and microwave heating. The samples were characterized by powder X-ray diffraction, (27)Al and (29)Si NMR spectroscopy. TEM and N(2) adsorption at -196 degrees C. The acidity of the samples and the space available inside the pores were evaluated through a catalytic model reaction, the isomerization of m-xylene, for which the profiles of the coke thermal decomposition were also analyzed. Powder X-ray diffraction and (29)Si and (27)Al MNR results show that in comparison with conventional heating, microwave irradiation (a less time consuming process) leads to identical amount of Si extraction from the zeolite framework. With this treatment. in addition to the customary mesopores development promoted by conventional heating, a partial conversion of the zeolite microporosity into larger micropores, is observed. The microwave irradiated and conventionally heated samples show different catalytic behavior in the m-xylene isomerization model reaction. It was observed that, by controlling the experimental conditions, it is possible to obtain samples with catalytic properties closer to the parent material, which is also confirmed by the respective coke analysis. (C) 2011 Elsevier B.V. All rights reserved.
Resumo:
Native agars from Gracilaria vermiculophylla produced in sustainable aquaculture systems (IMTA) were extracted under conventional (TWE) and microwave (MAE) heating. The optimal extracts from both processes were compared in terms of their properties. The agars’ structure was further investigated through Fourier transform infrared and NMR spectroscopy. Both samples showed a regular structure with an identical backbone, β-D-galactose (G) and 3,6-anhydro-α-L-galactose (LA) units; a considerable degree of methylation was found at C6 of the G units and, to a lesser extent, at C2 of the LA residues. The methylation degree in the G units was lower for MAEopt agar; the sulfate content was also reduced. MAE led to higher agar recoveries with drastic extraction time and solvent volume reductions. Two times lower values of [η] and Mv obtained for the MAEopt sample indicate substantial depolymerization of the polysaccharide backbone; this was reflected in its gelling properties; yet it was clearly appropriate for commercial application in soft-texture food products.
Resumo:
A empresa Petibol, S.A. – Embalagens de plástico centra-se na produção de embalagens de plástico a partir da matéria-prima Poliestireno Expandido (EPS) e Polipropileno Expandido (EPP). A empresa possui uma preocupação ao nível da qualidade da água e do aproveitamento energético, tendo desta forma surgido a realização do estudo na unidade industrial, com o objectivo de anular e/ou diminuir as possíveis lacunas existentes na unidade industrial. Numa primeira etapa foi realizada uma caracterização global à qualidade da água e à empresa, actualizando-se os esquemas já existentes, contabilizando-se os custos actuais relativamente aos processos no circuito da água (arrefecimento, aquecimento e pressurização), e por fim, efectuou-se um levantamento in loco do circuito de água, relativamente à pressão, temperatura e caudal. Numa fase posterior, foram propostos equipamentos e processos, tendo em vista a colmatação dos problemas identificados, realizando-se um subsequente estudo relativamente aos custos inerentes a esses novos processos. A caracterização à água foi avaliada em diferentes pontos do circuito industrial, tendo-se determinado na Sala de Bombagem que o filtro de areia não possuía as dimensões mais apropriadas, existindo também um problema a nível mecânico associado ao processo de contra-lavagem. Tais factos podem ser a causa da ocorrência de um aumento do teor de sólidos após a passagem na camada filtrante. Relativamente ao amaciador, este deveria amaciar de forma completa a água para alimentação à caldeira, embora se tenha registado à saída do amaciador uma dureza de 21,3 mg/L, denunciando problemas na troca iónica. No que toca à água de alimentação à caldeira, verifica-se a existência de parâmetros que não se encontram de acordo com os critérios enunciados para uma óptima qualidade, sendo eles o pH (10,14), condutividade (363 μS/cm), teor de ferro (1,21 mg/L) e a dureza (16 mg/L). De salientar que somente o teor de cobre, que se encontra em quantidades vestigiais, apresenta-se de acordo com os valores impostos. No que respeita à água da caldeira, esta apresenta parâmetros incompatíveis com os recomendados, sendo eles a condutividade (7350 μS/cm), teor de sólidos dissolvidos (5248 mg/L) e alcalinidade total (780 mg/L). De referir que o valor de pH (11,8) não se encontra de acordo com a aplicação do tratamento “fosfato-pH coordenado”. Em relação aos parâmetros com valores que se encontram dentro dos limites, estes correspondem à dureza (0 mg/L), ao teor de fosfatos (45 mg/L) e teor de sílica (0 mg/L). A água do circuito de arrefecimento foi sujeita a uma análise microbiológica, que corroborou a presença de um biofilme. Um dos problemas enunciados pela empresa, prendia-se com a impossibilidade de descarga, no colector municipal, dos condensados dos compressores, visto apresentarem uma quantidade de óleo de cerca de 43,3 mg/L, equivalente a quatro vezes o valor limite de emissão, de acordo com a legislação municipal. Por fim, o efluente de descarga industrial apresenta um valor de pH (10,3) acima do intervalo permitido por lei (6,0 – 9,0), sendo que a corrente que mais contribui para este acréscimo de pH corresponde à corrente proveniente da água de purga, visto esta apresentar um valor de pH de 12,22. De maneira a contornar os parâmetros enunciados, é proposto a substituição do filtro de areia da Sala de Bombagem, assim como a inserção de um conjunto de medidas de remoção de ferro e desinfecção, sendo a conjugação de arejamento, coagulação, filtração e desinfecção, por parte do hipoclorito, a proposta apresentada. Aos condensados dos compressores é apresentado um sistema de separação, que possibilita a remoção do óleo da água, e uma consequente descarga da mesma. Actualmente, não existe qualquer filtro de areia no circuito de arrefecimento da água, sendo proposto assim esse equipamento, de forma a minorar o desenvolvimento da população microbiana, bem como a permitir uma maior eficiência na transferência de calor na torre de arrefecimento. Relativamente à descarga industrial, é recomendável a colocação de um sistema de regularização automática de pH. A inserção de uma válvula de três vias permite um aproveitamento energético e de água, a partir da confluência da água oriunda dos furos com a água do tanque de água fria, sendo posteriormente alimentada à central de vácuo. No estudo da recuperação energética, um outro equipamento avaliado correspondeu à serpentina, no entanto, verificou-se que a poupança no consumo de gás natural era de apenas 0,005%, o que não se mostrou uma proposta viável. O orçamento de todos os equipamentos é de 11.720,76 €, possibilitando não só um melhor funcionamento industrial, como um menor impacto a nível ambiental. Os custos futuros de funcionamento aumentam em 3,36%, tendo a pressurização um aumento do seu custo em 3,4% em relação ao custo actual, verificando-se um custo anual de 10.781,21€, em relação aos processos de arejamento, coagulação e desinfecção.