870 resultados para Sistema de produção pesqueira


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O experimento teve como objetivo avaliar a distribuição das raízes do maracujazeiro-doce (Passiflora alata Dryand), cultivado em Nitossolo Vermelho, sob adubação química e orgânica, em Botucatu-SP. Foram utilizadas plantas com 19 meses de idade, em produção, conduzidas em latada e com irrigação. Os tratamentos com fertilizantes químicos e esterco de curral curtido foram os seguintes: T1 (400 g de sulfato de amônia), T2 (2,5kg de esterco), T3 (5,0kg de esterco), T4 (7,5kg de esterco) e T5 (10,0kg de esterco), acrescidos de 200g de termofosfato, 137g de cloreto de potássio e 2,0kg de calcário por planta, em todos os tratamentos, parcelados em duas aplicações. Foram empregadas 3 plantas por tratamento, sendo retiradas quatro amostras de cada uma, a 0-20 e 20-40cm de profundidade e distância do tronco. Os resultados evidenciaram que não houve diferenças significativas entre os tratamentos para massa seca das raízes. em todos os tratamentos, houve concentração das raízes a 0-20cm de distância do tronco. Nas parcelas com adubo orgânico, houve melhor distribuição das raízes em profundidade.

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A critical problem in mature gas wells is the liquid loading. As the reservoir pressure decreases, gas superficial velocities decreases and the drag exerted on the liquid phase may become insufficient to bring all the liquid to the surface. Liquid starts to drain downward, flooding the well and increasing the backpressure which decreases the gas superficial velocity and so on. A popular method to remedy this problem is the Plunger Lift. This method consists of dropping the "plunger"to the bottom of the tubing well with the main production valve closed. When the plunger reaches the well bottom the production valve is opened and the plunger carry the liquid to the surface. However, models presented in literature for predicting the behavior in plunger lift are simplistic, in many cases static (not considering the transient effects). Therefore work presents the development and validation of a numerical algorithm to solve one-dimensional compressible in gas wells using the Finite Volume Method and PRIME techniques for treating coupling of pressure and velocity fields. The code will be then used to develop a dynamic model for the plunger lift which includes the transient compressible flow within the well

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O cultivo consorciado de milho com forrageiras tropicais no sistema plantio direto na palha pode diminuir a incidência de plantas daninhas em decorrência da elevada produção de fitomassa e da alelopatia proporcionada pela deposição superficial de palha no solo. Este trabalho objetivou avaliar a influência da distribuição espacial da cultura do milho com Brachiaria brizantha, cultivados em consórcio no sistema plantio direto na palha, sobre a população de plantas daninhas. O experimento foi instalado em condições de campo, nos anos agrícolas 2002/03 e 2003/04, na Fazenda Experimental Lageado, em Botucatu-SP. O delineamento experimental foi o de blocos casualizados em esquema fatorial simples 2 x 4, com quatro repetições. Os tratamentos foram dois espaçamentos entre linhas de milho (E1-45 cm e E2- 90 cm) e quatro modalidades de cultivo (MCS - cultivo do milho solteiro; MBL - cultivo do milho com B. brizantha na linha de semeadura; BEM - cultivo do milho com B. brizantha na entrelinha; e MBLE - cultivo do milho com B. brizantha simultaneamente na linha e na entrelinha). Foram avaliados a produtividade de matéria seca da forrageira, a caracterização fitossociológica, a incidência e o controle de plantas daninhas. O cultivo MBLE a 90 cm foi a modalidade de consorciação que proporcionou maior produção de palhada. A presença de B. brizantha em cultivo consorciado diminuiu a densidade de plantas daninhas. A utilização do cultivo consorciado do milho com B. brizantha na linha+entrelinha proporcionou índice de controle de 95%, independentemente do espaçamento utilizado.

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

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

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O trabalho objetivou avaliar o efeito de diferentes manejos de água adotados na semeadura do arroz (Oryza sativa L.), em sistema pré-germinado, no estabelecimento das plantas e nos componentes vegetativos. O experimento foi conduzido no ano agrícola de 1995/96 em caixas de cimento amianto com capacidade de 500 L, contendo solo Aluvial Eutrófico de várzea, na Fazenda Experimental Lageado, no Município de Botucatu, SP. A cultivar empregada foi a IAC 102, e os tratamentos foram sete manejos de água. A semeadura de sementes pré-germinadas em solo saturado ou em lâmina de água limpa ou turva e sua retirada três dias após, apresentaram resultados semelhantes quanto à população e ao estabelecimento das plantas. A retirada da lâmina de água três dias após a semeadura resultou em maior população e fixação de plantas do que a permanência da lâmina por período maior de sete dias. A manutenção da lâmina da água limpa ou turva afetou a população de plantas e prejudicou o seu desenvolvimento inicial, causando seu estiolamento com significativa redução da produção de matéria seca. A turvação da água antes da semeadura reduziu o desenvolvimento e a população de plantas quando a lâmina de água não foi eliminada por evaporação ou retirada três dias após a semeadura.

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A adoção de técnicas que possibilitem a maximização da eficiência do uso de nitrogênio pelo feijoeiro é de extrema importância para aumentar a produtividade e qualidade de grãos, reduzir o custo de produção e evitar contaminação ambiental. O objetivo deste trabalho foi avaliar a resposta do feijoeiro (Phaseolus vulgaris L.) à aplicação de nitrogênio em cobertura nos estádios V4 e no início do R7, em sistema de plantio direto. O delineamento experimental foi em blocos ao acaso, em esquema fatorial 2 x 4, com quatro repetições. Os tratamentos foram constituídos pela aplicação de dois níveis de N (0 e 90 kg ha-1) no estádio V4, combinados com quatro níveis de N (0, 30, 60 e 120 kg ha-1) no início do estádio R7. Quando não foi realizada adubação nitrogenada de cobertura no estádio V4, a aplicação de N no início do estádio R7 aumentou a produtividade de grãos do feijoeiro em sistema de plantio direto. A produtividade máxima de grãos foi obtida com a aplicação exclusiva de 90 kg ha-1 de N no estádio V4, sendo necessárias, para atingir o mesmo nível de produtividade, maiores doses de N quando aplicadas apenas em R7. Quando é realizada aplicação de N em V4, adubações adicionais em R7 não resultam em aumento de produtividade. A aplicação de N em cobertura no estádio V4 foi mais eficiente do que a aplicação em R7, acarretando em maior incremento na produtividade por unidade do nutriente aplicado. A aplicação de N em cobertura, nos estádios V4 e início do R7, proporcionou aumento no teor de proteína nos grãos do feijoeiro.

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

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In vivo production of viral biopesticides is the major source of viral insecticides currently in the marketplace. However, this system presents limitations during production scale-up. For the Spodoptera frugiperda nucleopolyhedrovirus (SfMNPV), the insect used for replication has cannibalistic characteristics, thus production is even more difficult. Insect cells are commonly used for in vitro baculovirus production. Most of these cell lines are derived from Lepidoptera species. The Sf21 cell line is derived from Spodoptera frugiperda caterpillar ovarian tissue, and its clonal isolate Sf9 has been used for biopesticide production due to its ease of growth in suspension cultures. In this work, the in vitro production capabilities of a Brazilian SfMNPV isolate obtained from cornfields was evaluated. Comparison of polyhedra production was carried out using both Sf21 and Sf9 cells, based on volumetric and specific yields. Both cell lines were cultivated in Hyclone medium supplemented with different fetal bovine serum concentrations (2,5 and 5%). The best results were obtained using Sf9 cells supplemented with 5% serum. These results were further confirmed quantitively through kinetic parameter estimation for both cells lines and different serum concentrations. After seven successive passages, this system still presented high specific polyhedra production

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The production of petroleum is frequently accomplished with great volumes of water, that it is carried of the underground with the oil. It is a challenge of the present century the development of technologies that allow the use of waste water for purposes that consume great amounts of water and don't demand as rigid as the one of the drinking water requirements. The solar distillation has been configuring as an alternative of clean technology for desalination of brine and saline. Besides causing the minimum possible damage to the environment, it takes advantage of an abundant and free energy source: the solar energy. That study aims to develop a Solar Distillator for treatment of the produced water of the oil wells, to obtain an efluent to use in agriculture and vapor generation. The methodology for collection, conservation and analysis of the physical-chemical parameters obeyed the norms in APHA (1995). The sampling was of the composed type. Experiments were accomplished in the solar distillation pilot and simulation in thermostatic bathing. The operation was in batch system and for periods of 4, 6 and 12 h. The developed Distillator is of the type simple effect of two waters. It was still tested two inclination angles for covering; 20º and 45º. The Distillator presented minimum of 2,85 L/m2d revenues and maximum of 7,14 L/m2d. The removals of salts were great than 98%. The removal of TOC in the simulation was great than 90%. In agreement with the data of energy and mass balance, it was verified that the developed solar Distillator presented compatible revenues with those found in literature for similar types. It can be inferred that the obtained distilled water assists to the requirements CONAMA in almost all the points and could be used for irrigation of cultures such as cotton and mamona. As the distilled water has characteristics of fresh water it can be used in the generation of vapor

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The oil industry, experiencing a great economic and environmental impact, has increasingly invested in researches aiming a more satisfactory treatment of its largest effluent, i.e., produced water. These are mostly discarded at sea, without reuse and after a basic treatment. Such effluent contains a range of organic compounds with high toxicity and are difficult to remove, such as polycyclic aromatic hydrocarbons, salts, heavy metals, etc.. The main objective of this work was to study the solar distillation of produced water pre-treated to remove salts and other contaminants trough of a hybrid system with a pre-heater. This developed apparatus was called solar system, which consists of a solar heater and a conventional distillation solar still. The first device consisted of a water tank, a solar flat plate collector and a thermal reservoir. The solar distillator is of simple effect, with 1m2 of flat area and 20° of inclination. This dissertation was divided in five steps: measurements in the solar system, i.e. temperatures and distillate flow rate and weather data; modeling and simulation of the system; study of vapor-liquid equilibrium of the synthetic wastewater by the aqueous solution of p-xylene; physical and chemical analyses of samples of the feed, distillate and residue, as well as climatology pertinent variables of Natal-RN. The solar system was tested separately, with the supply water, aqueous NaCl and synthetic oil produced water. Temperature measurements were taken every minute of the thermal reservoir, water tank and distillator (liquid and vapor phases). Data of solar radiation and rainfall were obtained from INPE (National Institute for Space Research). The solar pre-heater demonstrated to be effective for the liquid systems tested. The reservoir fluid had an average temperature of 58°C, which enabled the feed to be pre-heated in the distillator. The temperature profile in the solar distillator showed a similar behavior to daily solar radiation, with temperatures near 70°C. The distillation had an average yield of 2.4 L /day, i.e., an efficiency of 27.2%. Mathematical modeling aided the identification of the most important variables and parameters in the solar system. The study of the vapor-liquid equilibrium from Total Organic Carbon (TOC) analysis indicated heteroazeotropia and the vapor phase resulted more concentrated in p-xylene. The physical-chemical analysis of pH, conductivity, Total Dissolved Solids (TDS), chlorides, cations (including heavy metals) and anions, the effluent distillate showed satisfactory results, which presents a potential for reuse. The climatological study indicates the region of Natal-RN as favorable to the operation of solar systems, but the use of auxiliary heating during periods of higher rainfall and cloud cover is also recommended

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Microalgae are microscopic photosynthetic organisms that grow rapidly and in different environmental conditions due to their simple cellular structure. The cultivation of microalgae is a biological system capable of storing solar energy through the production of organic compounds via photosynthesis, and these species presents growth faster than land plants, enabling higher biomass yield. Thus, it is understood that the cultivation of these photosynthetic mechanisms is part of a relevant proposal, since, when compared to other oil producing raw materials, they have a significantly higher productivity, thus being a raw material able to complete the current demand by biodiesel . The overall aim of the thesis was to obtain biofuel via transesterification process of bio oil from the microalgae Isochrysis galbana. The specific objective was to estimate the use of a photobioreactor at the laboratory level, for the experiments of microalgae growth; evaluating the characteristics of biodiesel from microalgae produced by in situ transesterification process; studying a new route for disinfection of microalgae cultivation, through the use of the chemical agent sodium hypochlorite. The introduction of this new method allowed obtaining the kinetics of the photobioreactor for cultivation, besides getting the biomass needed for processing and analysis of experiments in obtaining biodiesel. The research showed acceptable results for the characteristics observed in the bio oil obtained, which fell within the standards of ANP Resolution No. 14, dated 11.5.2012 - 18.5.2012. Furthermore, it was demonstrated that the photobioreactor designed meet expectations about study culture growth and has contributed largely to the development of the chosen species of microalgae. Thus, it can be seen that the microalgae Isochrysis galbana showed a species with potential for biodiesel production

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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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Pectinolytic enzymes, or simply pectinases, are complex enzymes that degrade pectic polymers. They have many uses, such as fruit juice extraction and purification, textile fiber treatment and vegetal oil extraction. The aim of this work was to study the kinetics of pectinases production by solid-state fermentation, using dry cashew apple residue as substrate and the microorganism Aspergillus niger CCT 0916. The influence of the initial medium moisture and medium supplementation with a source of nitrogen and phosphorus was evaluated using the factorial experimental planning and response surface methodology. Ammonia sulphate and potassium phosphate were used as nitrogen and phosphorus source, respectively. The variables time of contact (T) and ratio volume solvent/fermented medium (RZ), in systems with and without agitation, were evaluated in order to study the best extraction condition of the produced enzyme. Washed and unwashed cashew apple residues were tested as the growth medium. The unwashed residue was obtained by drying the residue after the extraction of the juice, while the washed residue was obtained by water washing 5 times using the proportion of 1 kg pulp/2 liters of water. Samples were taken every 12 hours for moisture content, pH, protein, reducing sugars, polygalacturonase activity (PG) and viscosity reduction. The physical-chemical composition of the residues had different sugar and pectin levels. For the unwashed residue, the peak activity was reached with 40% of initial moisture content, 1% of nitrogen supplementation without phosphorus addition after 30 hours of process. These conditions led to 16 U/g of PG activity and 82% of viscosity reduction. The calculated models reached similar values to the experimental ones in the same process conditions: 15.55 U/g of PG and 79.57% of viscosity eduction. Similarly, the greatest enzyme production for washed residue was reached with 40% initial moisture content, 1% nitrogen supplementation without phosphorus addition after 22 hours of cultivation. In this condition it was obtained polygalacturonase activity of 9.84 U/g and viscosity reduction of 81.36%. These values are close to experimental values that were of 10.1 U/g and 81%, respectively. The conditions that led to the best PG activity results was the agitated one and the best extraction condition was obtained with 100 minutes of solvent/medium contact and RZ of 5 (mL/g)