947 resultados para Líquido amniótico


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Esta pesquisa teve por objetivo geral discutir as abordagens teóricas do Patrimônio Líquido em função das diversas espécies de entidades ou empresas. Como objetivos específicos, procuramos responder às seguintes questões: l- Que abordagem teórica do Patrimônio Líquido e mais comumente aplicada nas diversas entidades no Brasil? 2- Qual o nível de conhecimento, por parte dos profissionais de contabilidade das empresas integrantes da pesquisa, a respeito das diversas formas de abordagens teóricas do Patrimônio Líquido? 3- Qual a utilidade das abordagens teóricas ao Patrimônio Líquido na vida das sociedades, ou das firmas individuais e/ou nas subsidiárias integrais? Ainda, é oportuno dizer que estudou-se o fluxo de informações contábeis associado aos diversos tipos de entidades e as diferentes espécies de abordagens teóricas ao Patrimônio Líquido. Citado fluxo foi investigado tanto do lado dos usuários que solicitam as informações, quanto dos profissionais de contabilidade que produzem as informações contábeis.

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Instituto Brasileiro de Economia

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Ionic liquids (ILs) are organic compounds liquid at room temperature, good electrical conductors, with the potential to form as a means for electrolyte on electrolysis of water, in which the electrodes would not be subjected to such extreme conditions demanding chemistry [1]. This paper describes the synthesis, characterization and study of the feasibility of ionic liquid ionic liquid 1-methyl-3(2,6-(S)-dimethyloct-2-ene)-imidazole tetrafluoroborate (MDI-BF4) as electrolyte to produce hydrogen through electrolysis of water. The MDI-BF4 synthesized was characterized by thermal methods of analysis (Thermogravimetric Analysis - TG and Differential Scanning Calorimetry - DSC), mid-infrared spectroscopy with Fourier transform by method of attenuated total reflectance (FTIR-ATR), nuclear magnetic resonance spectroscopy of hydrogen (NMR 1H) and cyclic voltammetry (CV). Where thermal methods were used to calculate the yield of the synthesis of MDI-BF4 which was 88.84%, characterized infrared spectroscopy functional groups of the compound and the binding B-F 1053 cm-1; the NMR 1H analyzed and compared with literature data defines the structure of MDI-BF4 and the current density achieved by MDI-BF4 in the voltammogram shows that the LI can conduct electrical current indicating that the MDI-BF4 is a good electrolyte, and that their behavior does not change with the increasing concentration of water

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Objetivou-se estudar o efeito da concentração de auxina e do meio líquido sobre o desenvolvimento de calos de cupuaçuzeiro. Segmentos de eixos embrionários e cotilédones, obtidos de frutos de cupuaçu dos tipos Mamorana e Redondo, foram cultivados em 4 meios de cultura diferentes: 1) meio MS (50%), suplementado com 2,4-D (1; 2; 4; 8 mg/L); 2) sais N6 (SIGMA) (4 g/L), acrescidos de 2,4-D (0; 2; 4 mg/L) e ANA (0; 3; 5 mg/L); 3) igual ao anterior, suplementado apenas com ANA (3 mg/L); e 4) meio MS, acrescido com ANA (1 mM). Calos com aspecto branco e brilhante foram observados em segmentos de eixos embrionários e cotilédones, cultivados nas menores concentrações de meio 1 (1 e 2 mg/L), enquanto nas maiores concentrações (4 e 8 mg/L) se observou a formação de calos e massa calosa branco-opaca, em eixos embrionários e em segmentos cotiledonares, estas estruturas tornaram-se escuras dentro de oito semanas. Usando o meio 2, um grande número de raízes foram formadas, enquanto o mesmo meio suplementado apenas com ANA (3; 5 mg/L) originou uma massa calosa. A combinação de ANA e 2,4-D, 3 e 2 mg/L, respectivamente, promoveu a formação de calos brancos e raízes. A transferência das culturas para meio líquido, sem regulador de crescimento, promoveu aumento de tamanho dos explantes e escurecimento dos mesmos. O cultivo desses explantes no meio 3 resultou no aparecimento de calos amarelos, com aspecto friável, que permaneceram com a mesma aparência no meio 4.

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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)

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Foram estudadas as características físico-químicas e citológicas do líquido sinovial da bainha tendínea digital de nove eqüinos hígidos. Verificou-se que o líquido é viscoso, amarelo claro, límpido, livre de partículas e que não coagula à temperatura ambiente. Sua concentração média de ácido hialurônico foi 60,20mg/dl, a taxa de glicose, similar à plasmática e sua concentração protéica não ultrapassou 1,74g/dl, com relação média albumina:globulina de 0,94. O número médio de células nucleadas foi de 313 células/µl, com predominância de grandes células mononucleares e linfócitos. Houve correlação significativa (r = - 0,649, P<0,01) entre o aumento da concentração de ácido hialurônico e a diminuição percentual de linfócitos. As mensurações das características pesquisadas no líquido sinovial da bainha tendínea digital de eqüinos são de execução simples e passíveis de implantação na rotina de atendimentos clínico-cirúrgicos.

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Unlike the already described techniques, which are based on imaginary lines among extremities or bone projections, this research describes a collection technique modification of cerebrospinal fluid (CSF) in dogs, in the atlantooccipital space. The palpation of bone structures in this joint, plus the supported directioning of the needle, does make the collection easy, even by professionals which have no experience in this kind of procedure. The applied technique enabled the collection of adequate volumes of limpid and colorless CSF of 50 healthy dogs in the first attempt of collection. There was no contamination with blood during the procedure, what made possible the correct interpretation of laboratory parameters usually examined in CSF samples.

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O dejeto líquido de suíno (DLS) pode constituir-se em excelente fonte de adubação em pastagem, com aplicação por aspersão, desde que seja assegurada a proteção do meio ambiente. Apesar de seu comprovado potencial para uso em sequeiro, pouco se conhece sobre o comportamento da cultivar Tifton 85 em sistemas sob irrigação e sob aplicação de DLS. Para determinar a produção de matéria seca pré-pastejo de Tifton 85 com DLS, foi conduzido um experimento na Fazenda-Escola da Universidade de Uberaba, irrigado por aspersão em malha, com aplicação de 0; 50; 100 e 200 m³ ha-1 ano-1 de DLS. Houve efeito significativo das doses de DLS em relação à produção de matéria seca pré-pastejo, ocorrendo acréscimos de produção com o aumento das doses. O fornecimento de 200 m³ ha-1 ano-1 de DLS possibilitou produção de 5.928 kg de matéria seca (MS) da forrageira por ciclo de 28 dias.

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Foram utilizados quatro bovinos mestiços, castrados, canulados no rúmen com o objetivo de quantificar as bactérias e protozoários líquido-associados, as bactérias sólido-aderidas e relacioná-las com o pH ruminal de bovinos recebendo amiréia dietética (30% de uréia) no concentrado e silagem de milho. Realizaram-se três coletas de conteúdo ruminal, à 1h, às 2h30 e 11h30 após a alimentação. A massa microbiana foi quantificada e qualificada nas diferentes frações das bactérias sólido-aderidas (BSA), bactérias líquido-associadas (BLA) e protozoários líquido-associados (PLA) e seus teores de nitrogênio (N), de matéria seca (MS) e de matéria orgânica (MO), determinados. A população microbiana apresentou crescente contribuição das BSA no decorrer do tempo, o que não ocorreu com BLA e PLA. O teor de MO/MS das BSA também aumentou o tempo 2h30, permanecendo inalterado até 11h30. Os teores de nitrogênio das BSA expressos na matéria orgânica diminuíram em tempos de coleta iguais ou superiores a 2h30, embora os teores de N na matéria seca não apresentassem essa diferença. As relações entre bactéria:protozoário encontradas foram iguais a 1 : 2,1 à 1 h, 2,6: 1 às 2h30 e 2,2: 1 às 11h30 após a alimentação, quando foi observado predomínio de protozoários e bactérias, ambos associados ao líquido ruminal. As quantidades totais e as frações do pool microbiano ruminal não foram influenciadas pelo pH, provavelmente, porque este se manteve sempre acima de 6,39.

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The great diversity of the textile industries activities causes the formation of wastewaters with high complex characteristics during the productive process, according to the industrial process used. The principal aim of the present work is the characterization of the wastewater from the textile industry that process the indigo, located in the Industrial District of Natal-RN, to know the contaminante load of each stage of the process and the framing of the wastewater with the standards of act of receiving of the System of Treatment of Wastewater of the Industrial District of Natal-RN SITEL-DIN, operated for the Company of Waters and Sewers of the RN CAERN. It was analyzed the following properties and pollutants agents: temperature; pH; alcalinity; color; COD (Chemical Oxygen Demand); total and suspended solids; heavy metals, thermotolerants coliformes, turbidity, dissolved oxygen and electrical conductivity. As conclusion it is distinguished that the wastewater did not get resulted satisfactory, according to comparisons with other sources, in only three parameters: turbidity, dissolved oxygen and electrical conductivity, however none of these parameters is criteria of acts of receiving of the SITEL-DIN,therefore the wastewater if finds inside of normality. After the analysis of the obtained results it was verified that SITEL-DIN is indispensable for completing the wastewater treatment

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Multiphase flows in ducts can adopt several morphologies depending on the mass fluxes and the fluids properties. Annular flow is one of the most frequently encountered flow patterns in industrial applications. For gas liquid systems, it consists of a liquid film flowing adjacent to the wall and a gas core flowing in the center of the duct. This work presents a numerical study of this flow pattern in gas liquid systems in vertical ducts. For this, a solution algorithm was developed and implemented in FORTRAN 90 to numerically solve the governing transport equations. The mass and momentum conservation equations are solved simultaneously from the wall to the center of the duct, using the Finite Volumes Technique. Momentum conservation in the gas liquid interface is enforced using an equivalent effective viscosity, which also allows for the solution of both velocity fields in a single system of equations. In this way, the velocity distributions across the gas core and the liquid film are obtained iteratively, together with the global pressure gradient and the liquid film thickness. Convergence criteria are based upon satisfaction of mass balance within the liquid film and the gas core. For system closure, two different approaches are presented for the calculation of the radial turbulent viscosity distribution within the liquid film and the gas core. The first one combines a k- Ɛ one-equation model and a low Reynolds k-Ɛ model. The second one uses a low Reynolds k- Ɛ model to compute the eddy viscosity profile from the center of the duct right to the wall. Appropriate interfacial values for k e Ɛ are proposed, based on concepts and ideas previously used, with success, in stratified gas liquid flow. The proposed approaches are compared with an algebraic model found in the literature, specifically devised for annular gas liquid flow, using available experimental results. This also serves as a validation of the solution algorithm

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The liquid of the rind of green coconut (LCCV), an effluent stream from the industrial processing of green coconut rind, is rich in sugars and is a suitable feedstock for fermentation. The first step of this study was to evaluate the potential of natural fermentation of LCCV. As the literature did not provide any information about LCCV and due to the difficulty of working with such an organic effluent, the second step was to characterize the LCCV and to develop a synthetic medium to explore its potential as a bioprocess diluent. The third step was to evaluate the influence of initial condensed and hydrolysable tannins on alcoholic fermentation. The last step of this work was divided into several stages: in particular to evaluate (1) the influence of the inoculum, temperature and agitation on the fermentation process, (2) the carbon source and the use of LCCV as diluent, (3) the differences between natural and synthetic fermentation of LCCV, in order to determine the best process conditions. Characterization of LCCV included analyses of the physico-chemical properties as well as the content of DQO, DBO and series of solids. Fermentation was carried out in bench-scale bioreactors using Saccharomyces cerevisiae as inoculum, at a working volume of 5L and using 0.30% of soy oil as antifoam. During fermentations, the effects of different initial sugars concentrations (10 - 20%), yeast concentrations (5 and 7.5%), temperatures (30 - 50°C) and agitation rates (400 and 500 rpm) on pH/sugars profiles and ethanol production were evaluated. The characterization of LCCV demonstrated the complexity and variability of the liquid. The best conditions for ethanol conversion were (1) media containing 15% of sugar; (2) 7.5% yeast inoculum; (3) temperature set point of 40°C and (4) an agitation rate of 500 rpm, which resulted in an ethanol conversion rate of 98% after 6 hours of process. A statistical comparison of results from natural and synthetic fermentation of LCCV showed that both processes are similar

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This work aims to use a different hydrodynamic condition applied to a new design of mixer-settler on treating wastewater produced by petroleum industry, called MDIF (Misturador-Decantador à Inversão de Fases/ Mixer-Settler based on Phase Inversion MSPI). The use of this different hydrodynamic behaviour is possible due to vertical disposition of the device and the principle of Phase Inversion that controls the MDIF, providing the generation (creation) of a cascade of drops, into an organic layer, that works as micro-decanters, thus making possible the formation of a bed of non-coalesced drops, called Bed Formation . The use of this new hydrodynamics condition allows to increase the residence time of the oil carrier drops, into an organic layer, and the device can treat a greater volume of wastewater. In view of to get this condition it is necessary to operate at high throughput (58,6 m3.m-2.h-1). By results, the condition of Bed Formation is the best one to be used when MSPI operates with throughput up to 58,6 m3.m-2.h-1. The results using the condition of Bed Formation show that increasing the height of the bed of non-coalesced drops and/or decreasing the volumetric ratio (O/A) an increase of the separation efficiency is detected