942 resultados para Equilíbrio (Fisologia)
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Partindo da premissa de que o estabelecimento do equilíbrio econômicofinanceiro inicial em contratos de concessão precisa se utilizar de teorias, conceitos e metodologias de outras ciências que não somente as ciências jurídicas, em especial das ciências econômicas e contábeis, a dissertação identifica as metodologias aplicáveis para a definição do conteúdo material da equação econômico-financeira inicial e as diferentes formas de quantificação dos limites e efeitos da verificação da ocorrência de riscos na alteração do equilíbrio econômico-financeiro original dos contratos de concessão.
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As parcerias entre o governo e instituições da sociedade civil têm se mostrado um instrumento fundamental para a consecução das políticas públicas. O “Programa Nacional de Publicização”, focalizando os serviços públicos não-exclusivos, trouxe maior possibilidade de flexibilização da gestão dessas atividades, chamando as organizações do terceiro setor a um papel de protagonismo na oferta de serviços públicos no Brasil. A nova interação entre esses agentes cria a necessidade de melhor entendimento de suas relações jurídicas e de realinhamento de expectativas e incentivos, bem como melhor definição da alocação de riscos entre os parceiros. Este trabalho analisa as parcerias com as Organizações Sociais na área da Cultura no Estado de São Paulo. Mais especificamente, o contrato de gestão da Fundação Osesp no período de 2005 a 2015. A partir desse caso, analisamos as oportunidades e dificuldades encontradas na contratualização dos resultados, os impactos na governança corporativa da instituição, as condições de alocação dos riscos, suas formas de mitigação e as necessidades de reequilíbrio econômico-financeiro.
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Unidade 1
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Identificar e analisar o comportamento motor em termos coordenativos em crianças dos 3 aos 6 anos de idade nos concelhos de Rio Maior e Santarém foi um dos nossos propósitos ao iniciar este processo científico. As crianças foram avaliadas com o teste MABC-2, exibindo os resultados do seu padrão motor coordenativo numa amostra representativa da população em causa. Com base nestes resultados analisámos o padrão motor coordenativo em função da idade, sexo, lateralidade. Observámos o comportamento das crianças com provável DCD e risco em termos da preferência e consistência da lateralidade. Posteriormente usando um teste de Midline Crossing procurámos analisar a dinâmica do uso da mão numa vertente de sistemas não lineares. Ainda nesta perspetiva teórica analisámos o equilíbrio, aspeto considerado preocupante nesta desordem para algumas crianças, através da análise de recorrência. Os instrumentos usados diferiram entre estudos em função dos objetivos de cada um: MABC-2, Midline Crossing, Questionário de Van Strien. Outro dos objetivos do nosso estudo recaiu no processo de intervenção junto de crianças em risco ou com provável desordem coordenativa no desenvolvimento. Em relação à nossa amostra encontrámos na literatura uma percentagem similar em termos de incidência de crianças com provável DCD e risco, por sexo e lateralidade. Constatámos que a percentagem de crianças com provável DCD apresenta uma representatividade percentual de acordo com a literatura. Existindo uma maior percentagem de sinistrómanos com provável DCD e do sexo masculino. Verificámos através dos sistemas não lineares que o comportamento das crianças com provável DCD se assemelha às crianças típicas, necessitando de um reforço na intervenção de forma a colmatar algumas das suas dificuldades. Verificámos que as crianças DCD são mais suscetíveis aos constrangimentos extrínsecos. Finalmente concluímos que a intervenção pode criar condições de excelência para modificar os padrões e perfis de comportamento.
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This study aimed at assessing the interobserver reliability of the Brazilian-Portuguese version of the Berg Balance Scale (BBS). The assessment was made by physiotherapists with extensive or little clinical experience in non-institutionalized elderly individuals. Participants comprised 12 elderly subjects (10 women and 2 men) with mean ages of 75.8 ± 8.4 years (range = 63-87) and 18 physiotherapists with varying clinical experience. Inter-examiner reliability obtained for each scale item yielded weighted kappa value > 0.75 in 11 of the 14 items (varying from 0.37 to 1.0). The intra-class correlation coefficient (ICC) for the total sum of BBS scores between the two groups of physiotherapists was 0.996 (95% confidence interval, 0.987 0.999) with a Cronbach alpha coefficient of 0.996. We found no difference between the rater groups when we compared the sum score means obtained with the student s T-test (p = 0.86). Although some items had low reliability values, in general our results suggest that the Brazilian Version of the BBS showed good levels of interrater reliability and agreement when used by physiotherapists with different clinical practice levels and without previous training on non-institutionalized elderly patients. We concluded that the BBS can be useful as an important evaluation instrument on a protocol for Rehabilitation clinics. It may be used by various health professionals, as: Physicians, Physical therapists, Physical educators, Occupational therapists, Nurses and Phonoaudiologists, so confirming the interdisciplinary character of this study
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Durante as últimas décadas, as indústrias farmacêuticas têm despertado grande interesse em óleos vegetais e vários extratos de planta por causa da sua baixa toxicidade e alta biodegrabilidade. O óleo de copaíba (Cop) é usado in natura na medicina popular como anti-inflamatório e antimicrobiano para tratar várias doenças, tais como inflamação da garganta, úlceras e infecções urinárias e pulmonares. Emulsões são sistemas dispersos termodinamicamente instáveis que consistem em dispersões de gotículas microscópicas em outro líquido imiscível. O objetivo deste trabalho foi preparar diferentes emulsões de Cop, determinar o EHL crítico deste óleo e avaliar a sua estabilidade, além de realizar estudos comparativos entre diferentes métodos de construção de diagramas de fases. As emulsões foram preparadas pelo método de inversão de fases variando as proporções de EHL de 4,7 a 16,7. A estabilidade foi determinada por vários métodos e os diagramas de fases foram produzidos pelo método de titulação usando diferentes procedimentos de agitação. As emulsões a base de Cop com EHL entre 12,7 e 15,7 foram as mais estáveis. As emulsões apresentaram boa estabilidade em curto e longo prazo, aspecto leitoso e baixos valores de índice de cremagem. Diferentes sistemas coloidais foram produzidos a partir dos diagramas de fases dependendo do processo de agitação. Baseado nesses métodos, o valor determinado de EHL do Cop foi 14,8, as emulsões permaneceram estáveis por mais de um ano e estes resultados indicam que o estudo das emulsões de Cop pode ser um promissor veículo de liberação tópica de fármacos e ativos cosméticos
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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)
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This paper analyzes the relationship between fundamental rights and the exercise of the claim punitive society in a democratic state. It starts with the premise that there are fundamental rights that limit and determine the validity of all forms of manifestation of the claim punitive society (legislating, investigative, adjudicative or ministerial) and there are others that require the state the right exercise, fast and effective of these activities. Travels to history in order to see that the first meaning of these rights was built between the seventeenth and eighteenth centuries, after all a history of abuses committed by state agents in the exercise of criminal justice, and positively valued in the declarations of human rights and proclaimed in the constitutions after the American and French Revolutions, while the second meaning has been assigned between the nineteenth and twentieth centuries, when, because of the serious social problems generated largely by absenteeism state, it was noted that in addition to subjective rights the individual against the state, fundamental rights are also objective values, which trigger an order directed the state to protect them against the action of the offending individuals themselves (duty to protect), the mission of which the State seeks to discharge, among other means, through the issue of legal rules typifying the behavior detrimental to such rights, subject to penalties, and the concrete actions of public institutions created by the Constitution to operate penal law. Under this double bias, it is argued that the rule violates the Constitution in the exercise of the claim punitive society as much as by excess malfere fundamental rights that limit, as when it allows facts wrong by offending fundamental rights, remain unpunished either by inaction or by insufficient measures taken abstractly or concretely provided
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Crude oil is a complex liquid mixture of organic and inorganic compounds that are dominated by hydrocarbons. It is a mixture of alkanes from the simplest to more complex aromatic compounds that are present derivatives such as gasoline, diesel, alcohol, kerosene, naphtha, etc.. These derivatives are extracted from any oil, however, only with a very high quality, in other words, when the content of hydrocarbons of low molecular weight is high means that production of these compounds is feasible. The American Petroleum Institute (API) developed a classification system for the various types of oil. In Brazil, the quality of most of the oil taken from wells is very low, so it is necessary to generate new technology to develop best practices for refining in order to produce petroleum products of higher commercial value. Therefore, it is necessary to study the thermodynamic equilibrium properties of its derivative compounds of interest. This dissertation aims to determine vapor-liquid equilibrium (VLE) data for the systems Phenilcyclohexane - CO2, and Cyclohexane - Phenilcyclohexane - CO2 at high pressure and temperatures between 30 to 70oC. Furthermore, comparisons between measured VLE experimental data from this work and from the literature in relation to the Peng- Robinson molecular thermodynamic model, using a simulation program SPECS IVCSEP v5.60 and two adjustable interaction parameters, have been performed for modeling and simulation purposes. Finally, the developed apparatus for determination of phase equilibrium data at high pressures is presented
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Anhydrous ethanol is used in chemical, pharmaceutical and fuel industries. However, current processes for obtaining it involve high cost, high energy demand and use of toxic and pollutant solvents. This problem occurs due to the formation of an azeotropic mixture of ethanol + water, which does not allow the complete separation by conventional methods such as simple distillation. As an alternative to currently used processes, this study proposes the use of ionic liquids as solvents in extractive distillation. These are organic salts which are liquids at low temperatures (under 373,15 K). They exhibit characteristics such as low volatility (almost zero/ low vapor ), thermal stability and low corrosiveness, which make them interesting for applications such as catalysts and as entrainers. In this work, experimental data for the vapor pressure of pure ethanol and water in the pressure range of 20 to 101 kPa were obtained as well as for vapor-liquid equilibrium (VLE) of the system ethanol + water at atmospheric pressure; and equilibrium data of ethanol + water + 2-HDEAA (2- hydroxydiethanolamine acetate) at strategic points in the diagram. The device used for these experiments was the Fischer ebulliometer, together with density measurements to determine phase compositions. The experimental data were consistent with literature data and presented thermodynamic consistency, thus the methodology was properly validated. The results were favorable, with the increase of ethanol concentration in the vapor phase, but the increase was not shown to be pronounced. The predictive model COSMO-SAC (COnductor-like Screening MOdels Segment Activity Coefficient) proposed by Lin & Sandler (2002) was studied for calculations to predict vapor-liquid equilibrium of systems ethanol + water + ionic liquids at atmospheric pressure. This is an alternative for predicting phase equilibrium, especially for substances of recent interest, such as ionic liquids. This is so because no experimental data nor any parameters of functional groups (as in the UNIFAC method) are needed
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Rio Grande do Norte, northeast state from Brazil, it is the greatest producer and exporter of yellow melon, well known as Spanish melon. Despite the consumption of this fruit to be mainly its pulp, melon seeds are an important source of lipids considered an industrial residue it has been discharge product. The use of oilseeds in order to produce biodiesel establishes an important raw material and the increase of its production promotes the national development of the agriculture. In this background, the aim of this work has been to use oil from seeds of yellow melon to produce biodiesel and to accomplish a study of the phase equilibrium of the system evolving biodiesel, methanol and glycerin. The biodiesel was obtained by oil transesterification through methylic route with molar ratio 1:9.7 (oil:alcohol) and with a mass of NaOH of 0.5% from the oil mass; the reaction time was 73 minutes at 55 °C. A yield of 84.94% in biodiesel was achieved. The equilibria data present a well-characterized behavior with a great region of two phases. The tie lines indicate that methanol has a best solubility in the phase that is rich in glycerin. Consistency of the experimental data was made based on Othmer-Tobias and Hand correlations which values above 0.99 were found to correlation coefficients, this fact confers a good thermodynamic consistency to the experimental data. NRTL and UNIQUAC models were employed to predict liquid-liquid equilibrium of this system. It was observed a better concordance of the results when NRTL was applied (standard deviation 1.25%) although the UNIQUAC model has presented a quite satisfactory result either (standard deviation 2.70%). The NRTL and UNIQUAC models were also used to evaluate the effect of temperature in the range of 328 K to 358 K, in which a little change in solubility with respect to the data obtained at 298 K was observed, thus being considered negligible the effect of temperature
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In the present work are established initially the fundamental relationships of thermodynamics that govern the equilibrium between phases, the models used for the description of the behavior non ideal of the liquid and vapor phases in conditions of low pressures. This work seeks the determination of vapor-liquid equilibrium (VLE) data for a series of multicomponents mixtures of saturated aliphatic hydrocarbons, prepared synthetically starting from substances with analytical degree and the development of a new dynamic cell with circulation of the vapor phase. The apparatus and experimental procedures developed are described and applied for the determination of VLE data. VLE isobarics data were obtained through a Fischer s ebulliometer of circulation of both phases, for the systems pentane + dodecane, heptane + dodecane and decane + dodecane. Using the two new dynamic cells especially projected, of easy operation and low cost, with circulation of the vapor phase, data for the systems heptane + decane + dodecane, acetone + water, tween 20 + dodecane, phenol + water and distillation curves of a gasoline without addictive were measured. Compositions of the equilibrium phases were found by densimetry, chromatography, and total organic carbon analyzer. Calibration curves of density versus composition were prepared from synthetic mixtures and the behavior excess volumes were evaluated. The VLE data obtained experimentally for the hydrocarbon and aqueous systems were submitted to the test of thermodynamic consistency, as well as the obtained from the literature data for another binary systems, mainly in the bank DDB (Dortmund Data Bank), where the Gibbs-Duhem equation is used obtaining a satisfactory data base. The results of the thermodynamic consistency tests for the binary and ternary systems were evaluated in terms of deviations for applications such as model development. Later, those groups of data (tested and approved) were used in the KijPoly program for the determination of the binary kij parameters of the cubic equations of state original Peng-Robinson and with the expanded alpha function. These obtained parameters can be applied for simulation of the reservoirs petroleum conditions and of the several distillation processes found in the petrochemistry industry, through simulators. The two designed dynamic cells used equipments of national technology for the determination of VLE data were well succeed, demonstrating efficiency and low cost. Multicomponents systems, mixtures of components of different molecular weights and also diluted solutions may be studied in these developed VLE cells
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The nonionic surfactants when in aqueous solution, have the property of separating into two phases, one called diluted phase, with low concentration of surfactant, and the other one rich in surfactants called coacervate. The application of this kind of surfactant in extraction processes from aqueous solutions has been increasing over time, which implies the need for knowledge of the thermodynamic properties of these surfactants. In this study were determined the cloud point of polyethoxylated surfactants from nonilphenolpolietoxylated family (9,5 , 10 , 11, 12 and 13), the family from octilphenolpolietoxylated (10 e 11) and polyethoxylated lauryl alcohol (6 , 7, 8 and 9) varying the degree of ethoxylation. The method used to determine the cloud point was the observation of the turbidity of the solution heating to a ramp of 0.1 ° C / minute and for the pressure studies was used a cell high-pressure maximum ( 300 bar). Through the experimental data of the studied surfactants were used to the Flory - Huggins models, UNIQUAC and NRTL to describe the curves of cloud point, and it was studied the influence of NaCl concentration and pressure of the systems in the cloud point. This last parameter is important for the processes of oil recovery in which surfactant in solution are used in high pressures. While the effect of NaCl allows obtaining cloud points for temperatures closer to the room temperature, it is possible to use in processes without temperature control. The numerical method used to adjust the parameters was the Levenberg - Marquardt. For the model Flory- Huggins parameter settings were determined as enthalpy of the mixing, mixing entropy and the number of aggregations. For the UNIQUAC and NRTL models were adjusted interaction parameters aij using a quadratic dependence with temperature. The parameters obtained had good adjust to the experimental data RSMD < 0.3 %. The results showed that both, ethoxylation degree and pressure increase the cloudy points, whereas the NaCl decrease