18 research outputs found

    Feira de Ciências e Ensino por Projetos: uma Experiência Educativa no Norte do Brasil

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    O objetivo do trabalho foi verificar quais contribuições que a feira de ciências propiciou na aprendizagem dos estudantes da Escola Estadual Presidente Costa e Silva (Gurupi – Tocantins) a partir da elaboração de projetos, além de identificar quais relações permearam essa aprendizagem. Todo o desenvolvimento dos trabalhos foi baseado na pesquisa participante. Os resultados da aplicação do questionário aos estudantes mostraram que a metodologia via projetos possibilitou a aquisição de diversos conhecimentos para elaborar, planejar e executar projetos voltados a problemas ambientais presentes no cotidiano. Ademais, observaram-se fortes características de interdisciplinaridade e contextualização em todos os projetos.  Assim, acredita-se que a realização de eventos deste tipo possa favorecer o desenvolvimento de muitas habilidades e competências, além de ser um espaço descontraído e agradável para expositores e visitantes, podendo ser classificado como um espaço não formal de educação

    Leishmania amazonensis promastigotes present two distinct modes of nucleus and kinetoplast segregation during cell cycle.

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    Abstract: Here, we show the morphological events associated with organelle segregation and their timing in the cell cycle of a reference strain of Leishmania (L.) amazonensis promastigotes, the main causative agent of Tegumentary leishmaniasis in the Americas. We show evidences that during the cell cycle, L. amazonensis promastigotes present two distinct modes of nucleus and kinetoplast segregation, which occur in different temporal order in different proportions of cells. We used DAPI-staining and EdU-labeling to monitor the segregation of DNA-containing organelles and DNA replication in wild-type parasites. The emergence of a new flagellum was observed using a specific monoclonal antibody. The results show that L. amazonensis cell cycle division is peculiar, with 65% of the dividing cells duplicating the kinetoplast before the nucleus, and the remaining 35% doing the opposite or duplicating both organelles concomitantly. In both cases, the new flagellum appeared during S to G2 phase in 1N1K cells and thus before the segregation of both DNA-containing organelles; however, we could not determine the exact timing of flagellar synthesis. Most of these results were confirmed by the synchronization of parasites using hydroxyurea. Altogether, our data show that during the cell cycle of L. amazonensis promastigotes, similarly to L. donovani, the segregation of nucleus and kinetoplast do not follow a specific order, especially when compared to other trypanosomatids, reinforcing the idea that this characteristic seems to be species-specific and may represent differences in cellular biology among members of the Leishmania genus

    Pervasive gaps in Amazonian ecological research

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    Pervasive gaps in Amazonian ecological research

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    Biodiversity loss is one of the main challenges of our time,1,2 and attempts to address it require a clear un derstanding of how ecological communities respond to environmental change across time and space.3,4 While the increasing availability of global databases on ecological communities has advanced our knowledge of biodiversity sensitivity to environmental changes,5–7 vast areas of the tropics remain understudied.8–11 In the American tropics, Amazonia stands out as the world’s most diverse rainforest and the primary source of Neotropical biodiversity,12 but it remains among the least known forests in America and is often underrepre sented in biodiversity databases.13–15 To worsen this situation, human-induced modifications16,17 may elim inate pieces of the Amazon’s biodiversity puzzle before we can use them to understand how ecological com munities are responding. To increase generalization and applicability of biodiversity knowledge,18,19 it is thus crucial to reduce biases in ecological research, particularly in regions projected to face the most pronounced environmental changes. We integrate ecological community metadata of 7,694 sampling sites for multiple or ganism groups in a machine learning model framework to map the research probability across the Brazilian Amazonia, while identifying the region’s vulnerability to environmental change. 15%–18% of the most ne glected areas in ecological research are expected to experience severe climate or land use changes by 2050. This means that unless we take immediate action, we will not be able to establish their current status, much less monitor how it is changing and what is being lostinfo:eu-repo/semantics/publishedVersio

    Rationale, study design, and analysis plan of the Alveolar Recruitment for ARDS Trial (ART): Study protocol for a randomized controlled trial

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    Background: Acute respiratory distress syndrome (ARDS) is associated with high in-hospital mortality. Alveolar recruitment followed by ventilation at optimal titrated PEEP may reduce ventilator-induced lung injury and improve oxygenation in patients with ARDS, but the effects on mortality and other clinical outcomes remain unknown. This article reports the rationale, study design, and analysis plan of the Alveolar Recruitment for ARDS Trial (ART). Methods/Design: ART is a pragmatic, multicenter, randomized (concealed), controlled trial, which aims to determine if maximum stepwise alveolar recruitment associated with PEEP titration is able to increase 28-day survival in patients with ARDS compared to conventional treatment (ARDSNet strategy). We will enroll adult patients with ARDS of less than 72 h duration. The intervention group will receive an alveolar recruitment maneuver, with stepwise increases of PEEP achieving 45 cmH(2)O and peak pressure of 60 cmH2O, followed by ventilation with optimal PEEP titrated according to the static compliance of the respiratory system. In the control group, mechanical ventilation will follow a conventional protocol (ARDSNet). In both groups, we will use controlled volume mode with low tidal volumes (4 to 6 mL/kg of predicted body weight) and targeting plateau pressure <= 30 cmH2O. The primary outcome is 28-day survival, and the secondary outcomes are: length of ICU stay; length of hospital stay; pneumothorax requiring chest tube during first 7 days; barotrauma during first 7 days; mechanical ventilation-free days from days 1 to 28; ICU, in-hospital, and 6-month survival. ART is an event-guided trial planned to last until 520 events (deaths within 28 days) are observed. These events allow detection of a hazard ratio of 0.75, with 90% power and two-tailed type I error of 5%. All analysis will follow the intention-to-treat principle. Discussion: If the ART strategy with maximum recruitment and PEEP titration improves 28-day survival, this will represent a notable advance to the care of ARDS patients. Conversely, if the ART strategy is similar or inferior to the current evidence-based strategy (ARDSNet), this should also change current practice as many institutions routinely employ recruitment maneuvers and set PEEP levels according to some titration method.Hospital do Coracao (HCor) as part of the Program 'Hospitais de Excelencia a Servico do SUS (PROADI-SUS)'Brazilian Ministry of Healt

    Pervasive gaps in Amazonian ecological research

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    Biodiversity loss is one of the main challenges of our time,1,2 and attempts to address it require a clear understanding of how ecological communities respond to environmental change across time and space.3,4 While the increasing availability of global databases on ecological communities has advanced our knowledge of biodiversity sensitivity to environmental changes,5,6,7 vast areas of the tropics remain understudied.8,9,10,11 In the American tropics, Amazonia stands out as the world's most diverse rainforest and the primary source of Neotropical biodiversity,12 but it remains among the least known forests in America and is often underrepresented in biodiversity databases.13,14,15 To worsen this situation, human-induced modifications16,17 may eliminate pieces of the Amazon's biodiversity puzzle before we can use them to understand how ecological communities are responding. To increase generalization and applicability of biodiversity knowledge,18,19 it is thus crucial to reduce biases in ecological research, particularly in regions projected to face the most pronounced environmental changes. We integrate ecological community metadata of 7,694 sampling sites for multiple organism groups in a machine learning model framework to map the research probability across the Brazilian Amazonia, while identifying the region's vulnerability to environmental change. 15%–18% of the most neglected areas in ecological research are expected to experience severe climate or land use changes by 2050. This means that unless we take immediate action, we will not be able to establish their current status, much less monitor how it is changing and what is being lost

    Development and economic analysis of 1G2G integrated biorefinery models using dilute acid pretreatment

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    O etanol é um dos biocombustíveis oriundos de fontes renováveis mais promissor e ambientalmente amigável. Visando-se ao atendimento de uma demanda crescente por este álcool, o aproveitamento integral dos materiais lignocelulósicos é uma alternativa interessante e, desta forma, trabalhos de pesquisa têm sido desenvolvidos visando-se à viabilização de biorrefinarias de produção integrada de etanol 1G e 2G. O presente trabalho teve como objetivo principal desenvolver e analisar economicamente modelos de biorrefinaria integrada 1G2G que empregam pré-tratamento ácido diluído, avaliando-se o impacto econômico do destino da hemicelulose para produção de etanol. Para isso, foram definidos cenários que incluíssem todas as etapas do processo de produção de etanol 1G e 2G, sendo avaliados dois teores de sólidos no reator de pré-tratamento (5% e 10%) e, para cada caso, três relações tempo e conversão da hidrólise enzimática, sendo estas de 45%, 51% e 55% para tempos de reação de 24h, 48h e 72h, respectivamente. Para cada condição, considerou-se a fermentação de pentose (C5) ou seu envio para tratamento de efluentes, constituindo-se, assim, 12 cenários. Foram realizadas as simulações destes cenários auxiliadas pelo pacote computacional Aspen Plus®, obtendo-se os dados de balanço de massa e energia, permitindo assim a realização da análise de viabilidade econômica empregando a plataforma Biorrefinaria Virtual de Cana - BVC. Foi possível observar que a produção de etanol 2G empregando pré-tratamento ácido diluído foi responsável por um aumento na produção de etanol de até 35%. Avaliando-se os cenários, observou-se que quando o reator de pré-tratamento foi operado com maior teor de sólidos, menor consumo de energia térmica foi necessário, requerendo menor quantidade de bagaço na caldeira e aumentando o rendimento final de etanol. Com relação ao custo de investimento, este correspondeu a R799,2milho~esparaabiorrefinaria1G,enquantoqueoscenaˊriosintegrados1G2Gapresentaramvalorescercade40799,2 milhões para a biorrefinaria 1G, enquanto que os cenários integrados 1G2G apresentaram valores cerca de 40% superiores. Dentre as áreas mais expressivas no custo de investimento, estão a de pré-tratamento e geração e distribuição de vapor. No que concerne ao custo de produção de etanol, os cenários que apresentaram menor valor para etanol 2G corresponderam ao uso de 10% de sólidos no reator de pré-tratamento com fermentação de C5. As áreas mais expressivas para esse custo foram os custos com insumos e capital. Todavia, os cenários com 5% de sólidos no reator de pré-tratamento e sem fermentação de C5 resultaram em menor custo de produção global de etanol (1G2G), sendo o custo com cana, insumos e capital os mais expressivos. Com base na taxa interna de retorno, esta se apresentou abaixo da taxa mínima de atratividade para todos os cenários, ocasionando um valor presente líquido negativo, inferindo-se que, nas condições avaliadas, a metodologia empregada nos cenários está inviável do ponto de vista de um investidor. No entanto, a análise econômica auxiliou a identificação dos gargalos tecnológicos do processo de produção integrada de etanol 1G2G quando estes empregam pré-tratamento ácido diluído, favorecendo a definição de metas operacionais a serem solucionadas em trabalhos de pesquisa.Ethanol is one of the most promising and environmentally friendly biofuels obtained from renewable energy sources. Aiming at meeting a growing demand for this fuel, the integral use of lignocellulosic materials is an interesting alternative and, in this way, research Works have been performed to make viable biorefineries for integrated production of 1G and 2G ethanol. The present work had as main objective to develop and to analyze economically models of 1G2G integrated biorefineries using dilute acid pretreatment, evaluating the economic impact of using hemicellulose for ethanol production. Alternative scenarios were defined including all steps of the 1G and 2G ethanol production process. Two different solids contents were evaluated in the pre-treatment reactor (5% and 10%) and, for each case, three values of time and conversion for the enzymatic hydrolysis step were considered, namely 45%, 51% and 55% for reaction times of 24h, 48h and 72h, respectively. For each condition, the fermentation of pentose (C5) or its sending for effluents treatment was supposed, constituting, thus, 12 scenarios. Simulations of these scenarios were carried out using the software Aspen Plus®, generating mass and energy balance data, thus allowing carrying out economic viability analysis using the Virtual Sugarcane Biorefinery (VSB) platform. Production of 2G ethanol using dilute acid pretreatment was responsible for an increase in ethanol production of up to 35%. When the pretreatment reactor was operated with higher solids content, lower thermal energy consumption was necessary, requiring less bagasse in the boiler and thus increasing the final ethanol yield. Regarding to investment cost, it was of R 799.2 million for 1G biorefinery, compared to a value 40% higher observed for integrated 1G2G scenarios. Among the most significant areas of investment cost are the pretreatment and the generation and distribution of steam. With relation to the cost of etanol production, scenarios that presented the lowest value for 2G ethanol corresponded to the use of 10% solids in the pre-treatment reactor associated to C5 fermentation. The most significant areas for this cost were the input and capital costs. However, the scenarios with 5% solids in the pre-treatment reactor without C5 fermentation resulted in a lower global ethanol production cost (1G2G), with sugarcane, chemical inputs and capital cost representing the most significant fraction. Based on the internal rate of return, this was lower than the minimum attractiveness rate of return for all scenarios, resulting in a negative net present value, allowing inferring that, under the evaluated conditions, the methodology used in the scenarios would be unviable from an investor viewpoint. However, the economic analysis helped to identify technological bottlenecks of the integrated 1G2G etanol production process using dilute acid pretreatment, favoring the definition of operational goals to be solved in research works

    Economic sustainability assessment of 1G2G integrated biorefineries with xylan and lignosulfonate co-production

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    As biorrefinarias surgem como matrizes industriais de processos sustentáveis com objetivo de empregar fontes renováveis na geração de bioprodutos. Essa abordagem renovável, no entanto, precisa ser atraente economicamente para que efetivamente substitua os processos não-renováveis. Assim, o presente trabalho teve como objetivo principal avaliar a sustentabilidade econômica de cenários de biorrefinarias integradas de produção de etanol 1G, etanol 2G e eletricidade, com a coprodução, individual e simultânea, de xilana e lignossulfonato, empregando cana-de-açúcar como matéria-prima. Para isso, foram definidos setes cenários, que incluíram a produção de etanol 1G e sua integração com a produção de etanol 2G, com subsequente integração da coprodução dos bioproduto, xilana e lignossulfonatos, tanto individualmente quanto simultaneamente. Para os cenários com produção de xilana, dois métodos de extração foram considerados, um por via biológica (enzimática) e outro por via química (hidróxido de sódio). Foram realizadas as simulações dos cenários com auxílio do software Aspen Plus®, obtendo-se os dados de balanço de massa e energia e, subsequentemente, sendo realizada a avaliação de sustentabilidade econômica. Para as xilanas, foi calculado o preço mínimo de venda (PMV) por meio de uma análise incremental. O rendimento da produção de etanol anidro e eletricidade excedente variaram de 81,1 a 105,87 L/TC e de 83 a 189,2 kWh/TC, respectivamente. Já a xilana e o lignossulfonatos tiveram rendimentos de 8,1 a 98,3 kg/TC e de 8,5 a 15,6 kg/TC, respectivamente. A coprodução individual de xilana na biorrefinaria 1G2G apresentou redução de 2,17% e 17,5% no rendimento de etanol e um aumento de 0% e 39,5% no excedente de eletricidade nas formas de extração enzimática e química, respectivamente. A fração de bagaço queimado foi largamente maior quando se empregou a via química para produção de xilana, resultado do maior consumo energético. A coprodução de lignossulfonatos na biorrefinaria 1G2G teve comportamento similar. Entretanto, os cenários com coprodução simultânea de xilana e lignossulfonatos apresentaram maiores vantagens sobre os cenários isolados. Com relação aos custos com investimento, a produção de xilana por via enzimática foi quase 4,5 vezes maior em comparação ao cenário da xilana obtida por via química. No cenário em que a taxa interna de retorno (TIR) correspondeu a 12% ao ano (valor presente líquido (VPL)=0), o PMV da xilana foi de R0,35eR0,35 e R4,38 para a produção por via enzimática e química, respectivamente. Para a coprodução de lignossulfonato, alcançou-se uma TIR anual de 13,22%, acompanhada de um VPL de aproximadamente R92milho~es.Entretanto,melhoresperspectivasecono^micasforamalcanc\cadasquandohouveacoproduc\ca~osimulta^neadosbioprodutos,aoobservarreduc\co~esde7792 milhões. Entretanto, melhores perspectivas econômicas foram alcançadas quando houve a coprodução simultânea dos bioprodutos, ao observar reduções de 77% e 14% no PMV para as xilanas por via enzimática e química, respectivamente. Ficou notória a contribuição da coprodução de xilana e lignossulfonatos em biorrefinarias com produção integrada de etanol 1G2G, tendo como pré-tratamento da biomassa o método de sulfito alcalino. Melhor desempenho econômico pode ser alcançado integrando coprodutos de maior valor agregado, o que também resulta no fomento da bioeconomia. Ademais, as análises permitiram a identificação dos gargalos tecnológicos, bem como a definição de metas operacionais a serem solucionadas em trabalhos de pesquisa.Biorefineries are emerging as industrial matrices of sustainable processes aiming to employ renewable sources in bioproduct generation. However, this renewable approach must be economically attractive to replace non-renewable processes effectively. Thus, the main objective of this study was to evaluate the economic sustainability of integrated biorefinery scenarios with 1G ethanol, 2G ethanol, and electricity production, and the, both individually and simultaneously, xylan and lignosulfonate co-production, using sugarcane as the feedstock. For this purpose, seven scenarios were defined, including the 1G ethanol production and its integration with the 2G ethanol production, followed by xylan and lignosulfonates coproduction, both individually and simultaneously. Two extraction methods were considered for the scenarios involving xylan production: biologically (enzymatic) and chemically (sodium hydroxide). The scenarios were simulated using the Aspen Plus® software, obtaining mass and energy balance data and conducting the economic sustainability assessment. The minimum selling price (MSP) for xylan was calculated through an incremental analysis. Anhydrous ethanol production and surplus electricity yields varied from 81.1 to 105.87 L/TC and 83 to 189.2 kWh/TC, respectively. Xylan and lignosulfonates had yields ranging from 8.1 to 98.3 kg/TC and 8.5 to 15.6 kg/TC, respectively. The xylan individual co-production in the 1G2G biorefinery showed a 2.17% and 17.5% reduction in ethanol yield and a 0% and 39.5% increase in surplus electricity for enzymatic and chemical extraction, respectively. Burnt bagasse fraction was significantly higher when the chemical route was employed for xylan production, as a result in higher energy consumption. Lignosulfonates co-production in the 1G2G biorefinery exhibited similar behavior. However, simultaneous co-production scenarios with xylan and lignosulfonates demonstrated greater advantages over individual scenarios. Regarding investment costs, the xylan enzymatic production was almost 4.5 times higher than the xylan obtained chemically. In the scenario where the internal rate of return (IRR) corresponded to 12% per year (net present value (NPV) = 0), the xylan MSP was R0.35 and R4.38forenzymaticandchemicalproduction,respectively.Approximately13.224.38 for enzymatic and chemical production, respectively. Approximately 13.22% annual IRR was achieved for lignosulfonate co-production, accompanied by R92 million NPV. However, better economic prospects were achieved when there were simultaneous coproduction bioproducts, resulting in 77% and 14% reductions in MSP for enzymatic and chemical xylans, respectively. The contribution of xylan and lignosulfonate co-production in biorefineries with 1G2G ethanol integrated production, utilizing the alkaline sulfite method as biomass pretreatment, was evident. Better economic performance can be achieved by integrating co-products with higher added value, which results also in fostering the bioeconomy. Furthermore, the analysis allowed the technological bottlenecks identification, as well as the operational goals definition, to be addressed in future research

    Patient-ventilator asynchrony

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    ABSTRACT Patient-v entilator asynchrony (PVA) is a mismatch between the patient, regarding time, flow, volume, or pressure demands of the patient respiratory system, and the ventilator, which supplies such demands, during mechanical ventilation (MV). It is a common phenomenon, with incidence rates ranging from 10% to 85%. PVA might be due to factors related to the patient, to the ventilator, or both. The most common PVA types are those related to triggering, such as ineffective effort, auto-triggering, and double triggering; those related to premature or delayed cycling; and those related to insufficient or excessive flow. Each of these types can be detected by visual inspection of volume, flow, and pressure waveforms on the mechanical ventilator display. Specific ventilatory strategies can be used in combination with clinical management, such as controlling patient pain, anxiety, fever, etc. Deep sedation should be avoided whenever possible. PVA has been associated with unwanted outcomes, such as discomfort, dyspnea, worsening of pulmonary gas exchange, increased work of breathing, diaphragmatic injury, sleep impairment, and increased use of sedation or neuromuscular blockade, as well as increases in the duration of MV, weaning time, and mortality. Proportional assist ventilation and neurally adjusted ventilatory assist are modalities of partial ventilatory support that reduce PVA and have shown promise. This article reviews the literature on the types and causes of PVA, as well as the methods used in its evaluation, its potential implications in the recovery process of critically ill patients, and strategies for its resolution

    Doença pulmonar por metal duro em trabalhador da indústria petrolífera

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    A doença pulmonar por metal duro é uma pneumonia intersticial por células gigantes relacionada com a exposição à poeira composta por metais duros. Neste artigo é relatado o caso de um profissional da indústria petrolífera, diagnosticado com doença pulmonar por metal duro com base na documentação clínica, radiológica, funcional pulmonar e anatomopatológica
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