Fontes e níveis de proteína em rações iniciais para leitões desmamados aos 21 dias de idade

Foi conduzido um experimento com o objetivo de avaliar fontes e níveis de proteína em rações iniciais para leitões desmamados aos 21 dias de idade. Utilizou-se um delineamento inteiramente casualizado em esquema fatorial 2 x 2 x 2, onde foram estudados os fatores: tipos de dieta (soro de leite em pó e farinha de peixe + lactose), níveis de proteína bruta (20,0% e 24,0%) e pesos dos leitões ao desmame (< 6,0 e > 6,0 kg), totalizando oito tratamentos com quatro repetições cada. O desempenho de leitões desmamados aos 21 dias de idade alimentados com rações contendo farinha de peixe + lactose foi superior ao dos leitões que consumiram apenas o soro de leite em pó. O nível de 24% de proteína bruta nas rações foi mais eficiente, sobretudo com a combinação farinha de peixe + lactose. Concluiu-se que os tipos de dietas estudados não exerceram efeito sobre os parâmetros histológicos e que a altura das vilosidades é uma função direta do peso do leitão.

Fontes de lactose, níveis de lisina dietéticos e peso dos leitões ao desmame

Desenvolveu-se um experimento com o objetivo de avaliar o uso de fontes de lactose (soro de leite em pó e lactose) e níveis de lisina em rações (1,20 e 1,50%), além do peso ao desmame (<6,0 e >6,0 kg), sobre o desempenho e a morfologia intestinal de 384 leitões desmamados com diferentes pesos e idade de 21 dias. Os leitões foram distribuídos em delineamento inteiramente casualizado em esquema fatorial 2 x 2 x 2, totalizando oito tratamentos em quatro repetições cada. Três leitões de cada tratamento foram abatidos aos 42 dias de idade, quando foram coletadas amostras do duodeno para estudo da morfologia intestinal. Foram avaliadas as características de desempenho ganho de peso, consumo de ração e conversão alimentar. Altura das vilosidades, profundidade de criptas duodenais e a relação altura de vilosidades/profundidade de criptas, bem como a relação peso do pâncreas/peso da carcaça, foram as características morfológicas avaliadas. O uso de lactose em rações à base de milho e farelo de soja proporcionou melhor desempenho dos leitões quando combinado a um nível de 1,5% de lisina. Concluiu-se ainda que os tipos de dietas estudados não exerceram efeito sobre a morfologia do duodeno e a relação peso do pâncreas/peso corporal e que a altura das vilosidades é uma função direta do peso do leitão.

Revisitando o problema de visibilidade para visualização tridimensional

We revisit the problem of visibility, which is to determine a set of primitives potentially visible in a set of geometry data represented by a data structure, such as a mesh of polygons or triangles, we propose a solution for speeding up the three-dimensional visualization processing in applications. We introduce a lean structure , in the sense of data abstraction and reduction, which can be used for online and interactive applications. The visibility problem is especially important in 3D visualization of scenes represented by large volumes of data, when it is not worthwhile keeping all polygons of the scene in memory. This implies a greater time spent in the rendering, or is even impossible to keep them all in huge volumes of data. In these cases, given a position and a direction of view, the main objective is to determine and load a minimum ammount of primitives (polygons) in the scene, to accelerate the rendering step. For this purpose, our algorithm performs cutting primitives (culling) using a hybrid paradigm based on three known techniques. The scene is divided into a cell grid, for each cell we associate the primitives that belong to them, and finally determined the set of primitives potentially visible. The novelty is the use of triangulation Ja 1 to create the subdivision grid. We chose this structure because of its relevant characteristics of adaptivity and algebrism (ease of calculations). The results show a substantial improvement over traditional methods when applied separately. The method introduced in this work can be used in devices with low or no dedicated processing power CPU, and also can be used to view data via the Internet, such as virtual museums applications

Localização de faltas em linhas de transmissão de múltiplos terminais a partir de registros oscilográficos sincronizados via transformada wavelet

The electric energy is essential to the development of modern society and its increasing demand in recent years, effect from population and economic growth, becomes the companies more interested in the quality and continuity of supply, factors regulated by ANEEL (Agência Nacional de Energia Elétrica). These factors must be attended when a permanent fault occurs in the system, where the defect location that caused the power interruption should be identified quickly, which is not a simple assignment because the current systems complexity. An example of this occurs in multiple terminals transmission lines, which interconnect existing circuits to feed the demand. These transmission lines have been adopted as a feasible solution to suply loads of magnitudes that do not justify economically the construction of new substations. This paper presents a fault location algorithm for multiple terminals transmission lines - two and three terminals. The location method is based on the use of voltage and current fundamental phasors, as well as the representation of the line through its series impedance. The wavelet transform is an effective mathematical tool in signals analysis with discontinuities and, therefore, is used to synchronize voltage and current data. The Fourier transform is another tool used in this work for extract voltage and current fundamental phasors. Tests to validate the location algorithm applicability used data from faulty signals simulated in ATP (Alternative Transients Program) as well as real data obtained from oscillographic recorders installed on CHESF s lines.

Enxertia em figueira 'Roxo de Valinhos' por borbulhia e garfagem

Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

Avaliação da secagem do bagaço de cajá usando planejamento fatorial composto central

This work deals with the kinetics assay of Cajá (Spondias mombin L.) bagasse drying by an experimental design using a tray dryer. In order to add-value to this product a kinetic study has been carried out. A central composite experimental design has been carried out to evaluate the influence of the operational variables: input air temperature (55; 65 e 75ºC); the drying air velocity (3.2; 4.6 e 6.0 m/s) and the fixed bed thickness (0.8; 1.2 e 1.6 cm) and as response variable the the moisture content (dry basis). The results showed that the diffusional Fick model fitted quite well the experimental data. The best condition found has been input air temperature of 75ºC, drying air velocity of 6.0 m/s as well as fixed bed thickness of 0.8 cm. The experimental design assay showed that the main effects as well as the second ones were significant at 95% confindance level. The best operational condition according to statistical planning was 75 oC input air temperature, 6.0 m.s-1 drying air velocity and 0.8 cm fixed bed thickness. In this case, the equilibrium moisture content (1.3% dry basis) occured at 220 minutes

Levantamento de plantas aquáticas no reservatório de Salto Grande, Americana-SP

O objetivo deste estudo foi determinar a frequência relativa e o nível de infestação de cada espécie da flora aquática presente no reservatório de Salto Grande, Americana-SP. O levantamento e a identificação das plantas aquáticas foram realizados percorrendo-se as margens do reservatório em uma embarcação. Ao longo dele foram estabelecidos 20 pontos de avaliação, sendo todos eles fotografados e georreferenciados. Foram atribuídos valores de 0 a 100% tanto para as espécies presentes como para os espaços livres de macrófitas aquáticas que eventualmente pudessem ocorrer dentro dos pontos amostrados. Com os dados referentes ao número de indivíduos e pontos avaliados, foi determinada a frequência relativa de cada espécie. Foram identificadas 13 espécies em todo o reservatório, sendo 12 vasculares e uma de alga-verde (Chlorella spp.). Entre as espécies vasculares, nove eram plantas emersas flutuantes, as quais poderiam estar ou não ancoradas no leito do reservatório: Alternanthera philoxeroides, Brachiaria subquadripara, Cyperus difformis, Echinochloa polystachia var. spectabilis, Eichhornia crassipes, Panicum rivulare, Pistia stratiotes, Salvinia auriculata e Typha angustifolia. Outras três espécies foram encontradas somente em solo firme alagado: Aeschynomene sensitiva, Hedychium coronarium e Mimosa pigra.

Estudo da movimentação de plantas aquáticas imersas presentes no reservatório da UHE Eng. Souza Dias - Jupiá

O objetivo deste estudo foi desenvolver um método para determinação de pontos de reprodução e de suas respectivas importâncias na disseminação das espécies E. densa, E. najas e C. demersum no reservatório de Jupiá. Foram monitorados dez locais nos quais se encontrou registro de altas infestações dessas espécies. Dois desses locais situam-se no rio Paraná, nas lagoas denominadas de Ferradura e Pernilongo; os outros oito sítios estão localizados no rio Tietê, nas lagoas marginais Testemunha, Barrenta, Vírgula e Flórida, e no leito do rio nos pontos Acima da Ponte dos Barrageiros, Abaixo da Ponte, Baía ao Lado da Ponte e em frente da Praia de Itapura. em cada um desses sítios de reprodução foram liberados e monitorados dez blocos de plantas aquáticas imersas por mês. Os blocos possuíam volume de 0,14 cm³ e receberam uma etiqueta plástica de identificação externa e uma bóia de cor laranja, com o objetivo de serem facilmente localizadas ou visualizadas à distância. Após a soltura, cada bloco foi georreferenciado por meio de um aparelho GPS, sendo o seu deslocamento avaliado a cada 15 dias. Os sítios Lagoa Vírgula, Lagoa Testemunha e Lagoa Barrenta destacaram-se quanto ao número de blocos (30, 20 e 19 blocos, respectivamente), que percorreram distâncias superiores a 500 m e, conseqüentemente, saíram de seus respectivos locais de reprodução. A grande maioria dos blocos permaneceu dentro da Lagoa Flórida; somente 12 blocos saíram e alcançaram o leito do rio Tietê. O sítio denominado Leito Acima da Ponte foi o que mais se destacou dentre os três localizados no leito do rio Tietê, pois forneceu 18 blocos de plantas, enquanto os sítios Abaixo da Ponte e Baía ao Lado da Ponte forneceram 15 e 14 blocos, respectivamente. O sítio Praia de Itapura foi o que apresentou menor importância em relação ao fornecimento de plantas imersas no rio Tietê, sendo localizadas apenas 11 bóias com deslocamento superior a 500 m. Os sítios de reprodução localizados no rio Paraná também contribuíram para o fornecimento de plantas imersas ao reservatório de Jupiá; nove blocos saíram da Lagoa Pernilongo e apresentaram deslocamentos superiores a 500 m. Entretanto, os sítios Lagoa Barrenta e Lagoa Ferradura foram aqueles que mais contribuíram com a chegada de plantas na tomada de água da UHE Eng. Souza Dias, uma vez que foram recolhidos, respectivamente, seis e quatro blocos de plantas provenientes desses locais de dispersão. A metodologia utilizada mostrou-se eficaz quanto à avaliação da movimentação de plantas aquáticas imersas dentro do reservatório de Jupiá.

Extração do óleo essencial de Cymbopogom winterianus J. com CO2 pressurizado

The extraction with pressurized fluids has become an attractive process for the extraction of essential oils, mainly due the specific characteristics of the fluids near the critical region. This work presents results of the extraction process of the essential oil of Cymbopogon winterianus J. with CO2 under high pressures. The effect of the following variables was evaluated: solvent flow rate (from 0.37 to 1.5 g CO2/min), pressure (66.7 and 75 bar) and temperature (8, 10, 15, 20 and 25 ºC) on the extraction kinetics and the total yield of the process, as well as in the solubility and composition of the C. winterianus essential oil. The experimental apparatus consisted of an extractor of fixed bed and the dynamic method was adopted for the calculation of the oil solubility. Extractions were also accomplished by conventional techniques (steam and organic solvent extraction). The determination and identification of extract composition were done by gas chromatography coupled with a mass spectrometer (GC-MS). The extract composition varied in function of the studied operational conditions and also related to the used extraction method. The main components obtained in the CO2 extraction were elemol, geraniol, citronellol and citronellal. For the steam extraction were the citronellal, citronellol and geraniol and for the organic solvent extraction were the azulene and the hexadecane. The most yield values (2.76%) and oil solubility (2.49x10-2 g oil/ g CO2) were obtained through the CO2 extraction in the operational conditions of T = 10°C, P = 66.7 bar and solvent flow rate 0.85 g CO2/min

Enraizamento de estacas apicais de figueira Roxo de Valinhos submetidas à estratificação a frio úmido e AIB

Na produção de mudas de figueira a utilização de estacas apicais de menor comprimento pode facilitar o manejo no viveiro, entretanto ainda não foram definidos os protocolos para enraizamento desse tipo de estaca. O objetivo do presente trabalho foi avaliar a ação da estratificação à frio úmido e do tratamento com AIB na rizogênese de estacas apicais de figueira Roxo de Valinhos. As estacas foram coletadas da porção apical dos ramos no final do período hibernal (julho) e padronizadas com 20 cm de comprimento e diâmetro aproximado de 0,7 cm. As estacas foram estratificadas (estacas embrulhadas em jornal umedecido e protegidas com saco plástico à temperatura de 4 ºC, em câmara tipo BOD) por diferentes períodos (0, 15, 30, 45 e 60 dias) e, posteriormente, tratadas e não tratadas com 2.000 mg L-1 de AIB por 10 segundos. em seguida, as estacas foram enterradas em leito de areia umedecido sob telado constituído de tela de polipropileno preta (sombreamento de 50%). Passados 60 dias de cada período de estratificação, foram mensuradas a percentagem de estacas enraizadas, a percentagem de estacas brotadas e o número médio de brotações e de raízes por estaca. Conclue-se que as estacas apicais de figueira Roxo de Valinhos estratificadas a frio úmido por 30 dias e posteriormente tratadas com 2.000 mg L-1 de AIB apresentaram maior potencial de rizogênese.

Estudo da hidrodinâmica de um novo separador líquido-líquido: aplicação ao sistema óleo-bruto/água produzida

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

Planejamento experimental aplicada a um novo separador líquido-líquido utilizado no tratamento de águas residuais contaminadas com petróleo

The present work had as objective to apply an experimental planning aiming at to improve the efficiency of separation of a new type of mixer-settler applied to treat waste water contaminated with oil. An unity in scale of laboratory, was installed in the Post-graduation Program of Chemical Engineering of UFRN. It was constructed in partnership with Petrobras S.A. This called device Misturador-Decantador a Inversão de Fases (MDIF) , possess features of conventional mixer-settler and spray column type. The equipment is composed of three main parts: mixing chamber; chamber of decantation and chamber of separation. The efficiency of separation is evaluated analyzing the oil concentrations in water in the feed and the output of the device. For the analysis one used the gravimetric method of oil and greases analysis (TOG). The system in study is a water of formation emulsified with oil. The used extractant is a mixture of Turpentine spirit hydro-carbons, supplied for Petrobras. It was applied, for otimization of the efficiency of separation of the equipment, an experimental planning of the composite central type, having as factorial portion fractionary factorial planning 2 5-2, with the magnifying of the type star and five replications in the central point. In this work, the following independents variables were studied: contents of oil in the feed of the device; volumetric ratio (O/A); total flowrate ; agitation in the mixing chamber and height of the organic bed. Minimum and maximum limits for the studied variables had been fixed according previous works. The analysis of variance for the equation of the empirical model, revealed statistically significant and useful results for predictions ends. The variance analysis also presented the distribution of the error as a normal distribution and was observed that as the dispersions do not depend on the levels of the factors, the independence assumption can be verified. The variation around the average is explained by 98.98%, or either, equal to the maximum value, being the smoothing of the model in relation to the experimental points of 0,98981. The results present a strong interaction between the variable oil contents in the feed and agitation in the mixing chamber, having great and positive influence in the separation efficiency. Another variable that presented a great positive influence was the height of the organic bed. The best results of separation efficiency had been obtained for high flowrates when associates the high oil concentrations and high agitation. The results of the present work had shown excellent agreement with the results carried out through previous works with the mixer-settler of phase inversion

Síntese e caracterização do carbeto de molibdênio nanoestruturado para fins catalíticos na reação de oxidação parcial do metano

The nanostructures materials are characterized to have particle size smaller than 100 nm and could reach 1 nm. Due to the extremely reduced dimensions of the grains, the properties of these materials are significantly modified relatively when compared with the conventional materials. In the present work was accomplished a study and characterization of the molybdenum carbide, seeking obtain it with particles size in the nanometers order and evaluate its potential as catalyst in the reaction of partial methane oxidation. The method used for obtaining the molybdenum carbide was starting from the precursor ammonium heptamolybdate of that was developed in split into two oven, in reactor of fixed bed, with at a heating rate of 5ºC/min, in a flow of methane and hydrogen whose flow was of 15L/h with 5% of methane for all of the samples. The studied temperatures were 350, 500, 600, 650, 660, 675 and 700ºC and were conducted for 0, 60, 120 and 180 minutes, and the percent amount and the crystallite size of the intermediate phases were determined by the Rietveld refinement method. The carbide obtained at 660ºC for 3 hours of reaction showed the best results, 24 nm. Certain the best synthesis condition, a passivating study was accomplished, in these conditions, to verify the stability of the carbide when exposed to the air. The molybdenum carbide was characterized by SEM, TEM, elemental analysis, ICP-AES, TG in atmosphere of hydrogen and TPR. Through the elemental analysis and ICP-AES the presence carbon load was verified. TG in atmosphere of hydrogen proved that is necessary the passivating of the molybdenum carbide, because occur oxidation in room temperature. The catalytic test was accomplished in the plant of Fischer-Tropsch of CTGAS, that is composed of a reactor of fixed bed. Already the catalytic test showed that the carbide presents activity for partial oxidation, but the operational conditions should be adjusted to improve the conversion

Avaliação do processo oxidativo avançado por permanganato de potássio no tratamento de solos contaminados com idrocarbonetos poliaromáticos

The soil contamination with petroleum is one of the major concern of industries operating in the field and also of environmental agencies. The petroleum consists mainly of alkanes and aromatic hydrocarbons. The most common examples of hydrocarbons polyaromatic are: naphthalene, anthracene, phenanthrene, benzopyrene and their various isomers. These substances cause adverse effects on human and the environment. Thus, the main objective of this work is to study the advanced oxidation process using the oxidant potassium permanganate (KMnO4) for remediation of soils contaminated with two polyaromatic hydrocarbons (PAHs): anthracene and phenanthrene. This study was conducted at bench scale, where the first stage was at batch experiment, using the variables: the time and oxidant dosage in the soil. The second stage was the remediation conducted in continous by a fix column, to this stage, the only variable was remediation time. The concentration of oxidant in this stage was based on the best result obtained in the tests at batch, 2,464 mg / L. The results of degradation these contaminants were satisfactory, at the following dosages and time: (a) 5g of oxidant per kg soil for 48 hours, it was obtained residual contaminants 28 mg phenanthrene and 1.25 mg anthracene per kg of soil and (b) for 7g of oxidant per kg soil in 48 hours remaining 24 mg phenanthrene and anthracene 0.77 mg per kg soil, and therefore below the intervention limit residential and industrial proposed by the State Company of Environmental Sao Paulo (CETESB)

Avaliação da capacidade de adsorção do CO2 em zeólita 12X com gases sintéticos e originados da pirólise do lodo de esgoto

This work depicts a study of the adsorption of carbon dioxide on zeolite 13X. The activities were divided into four stages: study batch adsorption capacity of the adsorbent with synthetic CO2 (4%), fixed bed dynamic evaluation with the commercial mixture of gases (4% CO2, 1.11% CO, 1 2% H2, 0.233% CH4, 0.1% C3, 0.0233% C4 argon as inert closing balance), fixed bed dynamic modeling and evaluation of the breakthrough curve of CO2 originated from the pyrolysis of sewage sludge. The sewage sludge and the adsorbent were characterized by analysis TG / DTA, SEM, XRF and BET. Adsorption studies were carried out under the following operating conditions: temperature 40 °C (for the pyrolysis of the sludge T = 600 °C), pressures of 0.55 to 5.05 bar (batch process), flow rate of the gaseous mixture between 50 - 72 ml/min and the adsorbent masses of 10, 15 and 20 g (fixed bed process). The time for the adsorption batch was 7 h and on the fixed bed was around 180 min. The results of this study showed that in batch adsorption process step with zeolite 13X is efficient and the mass of adsorbed CO2 increases with the increases pressure, decreases with temperature increases and rises due the increase of activation temperature adsorbent. In the batch process were evaluated the breakthrough curves, which were compared with adsorption isotherms represented by the models of Langmuir, Freündlich and Toth. All models well adjusted to the experimental points, but the Langmuir model was chosen in view of its use in the dynamic model does not have implications for adsorption (indeterminacy and larger number of parameters such as occurred with others) in solving the equation. In the fixed bed dynamic study with the synthetic gas mixture, 20 g of mass adsorbent showed the maximum adsorption percentage 46.7% at 40 °C temperature and 50 mL/min of flow rate. The model was satisfactorily fitted to the three breakthrough curves and the parameters were: axial dispersion coefficient (0.0165 dm2/min), effective diffusivity inside the particle (dm2/min 0.0884) and external transfer coefficient mass (0.45 dm/min). The breakthrough curve for CO2 in the process of pyrolysis of the sludge showed a fast saturation with traces of aerosols presents in the gas phase into the fixed bed under the reaction process