Clonagem de quatro espécies de Annonaceae potenciais como porta-enxertos

O trabalho objetivou o estudo da capacidade de enraizamento de quatro espécies de Annonaceae potenciais como porta-enxertos (Annona glabra L., Annona montana Macfad, Rollinia emarginata e Rollinia mucosa Baill.) em três épocas do ano (verão, outono e inverno). Experimento conduzido em câmara de nebulização intermitente pertencente à UNESP/FCAV (21º15'22S e 48º18'58W), utilizando-se de estacas apicais enfolhadas em tratamento rápido (5 segundos) com ácido indolbutírico (IBA) (0; 1000; 3000; 5000 e 7000 mg.L-1), em esquema fatorial. Após 90 dias, avaliaram-se a porcentagem de estacas enraizadas, sobrevivência, comprimento e número de raízes. Como resultados, o IBA não incrementou a capacidade de enraizamento das espécies. A época do ano foi grande influente no sucesso de enraizamento, sendo o verão mais adequado. A. glabra e A. montana mostraram-se promissoras na propagação vegetativa via estaquia (clonagem). R. emarginata apresentou baixos valores para as características avaliadas, devendo ser intensificados experimentos na promoção do enraizamento em relação aos atuais valores obtidos. R. mucosa não apresentou resultados satisfatórios, ocorrendo necrose de tecido na base das estacas, devendo as causas serem melhor investigadas. O sucesso no enraizamento de Annonaceae é dependente da espécie, tendo aquelas do gênero Annona apresentado resultados superiores em relação às do gênero Rollinia.

Influência do ácido indolbutírico no enraizamento de estacas apicais e basais de caramboleira (Averrhoa carambola L.) sob condições de nebulização intermitente

A produção de mudas de caramboleira é um dos fatores limitantes à expansão comercial da cultura, devido ao tempo que estas levam para serem formadas e iniciarem a produção. Uma boa alternativa pode estar na otimização dos métodos de propagação vegetativa, através de estudos relativos aos processos e fatores envolvidos no enraizamento de estacas. Este trabalho foi desenvolvido com o objetivo de estudar o enraizamento de estacas apicais e basais de caramboleira, tratadas com ácido indolbutírico (IBA), em condições de nebulização intermitente. Estacas apicais e basais de caramboleira foram coletadas de ramos de plantas-matrizes da cultivar B-10 e submetidas à aplicação de cinco concentrações de IBA (0; 1.000; 3.000; 5.000 e 7000 mg.L-1), em imersão por 10 segundos, para avaliar a capacidade de sobrevivência, enraizamento e número médio de raízes/estaca. Posteriormente, as estacas foram colocadas em caixas de madeira contendo vermiculita média como substrato e mantidas em casa de vegetação, sob nebulização intermitente, durante 70 dias. O delineamento experimental utilizado foi em esquema fatorial 2 x 5, com 4 repetições e 10 estacas/parcela. As estacas apicais obtiveram melhores resultados para porcentagem de sobrevivência (49,26%), enraizamento (34,84%) e número médio de raízes (20,51), mostrando-se superiores às basais. O uso de IBA não influenciou em nenhuma das variáveis analisadas.

Insect Venom Peptides

The insects of the order Hymenoptera ( bees, wasps, and ants) are classified in two groups, based on their life history: social and solitary. The venoms of the social Hymenoptera evolved to be used as defensive tools to protect the colonies of these insects from the attacks of predators. Generally they do not cause lethal effects but cause mainly inflammatory and/or immunological reactions in the victims of their stings. However, sometimes it is also possible to observe the occurrence of systemic effects like respiratory and/or kidney failure. Meanwhile, the venoms of solitary Hymenoptera evolved mainly to cause paralysis of the preys in order to permit egg laying on/within the prey's body; thus, some components of these venoms cause permanent/transient paralysis in the preys, while other components seem to act preventing infections of the food and future progenies. The peptide components of venoms from Hymenoptera are spread over the molar mass range of 1400 to 7000 da and together comprise up to 70% of the weight of freeze-dried venoms. Most of these toxins are linear polycationic amphipatic peptides with a high content of alpha-helices in their secondary structures. These peptides generally account for cell lysis, hemolysis, antibiosis, and sometimes promote the delivery of cellular activators/mediators through interaction with the G-protein receptor, and perhaps some of them are even immunogenic components. In addition to these peptides, the Hymenopteran venoms also may contain a few neurotoxins that target Na+ and/or Ca+2 channels or even the nicotinic ACh receptor. This review summarizes current knowledge of the biologically active Hymenoptera venoms.

Bandoniozyma gen. nov., a Genus of Fermentative and Non-Fermentative Tremellaceous Yeast Species

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

Performance of an Anaerobic Baffled Reactor (ABR) in treatment of cassava wastewater

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

Composition-resolved size distributions of volcanic aerosols in the Mt. Etna plumes

Particle size distributions for soluble and insoluble species in Mt. Etna's summit plumes were measured across an extended size range (10 nm < d < 100 mu m) using a combination of techniques. Automated scanning electron microscopy (QEMSCAN) was used to chemically analyze many thousands of insoluble particles (collected on pumped filters) allowing the relationships between particle size, shape, and composition to be investigated. The size distribution of fine silicate particles (d < 10 mu m) was found to be lognormal, consistent with formation by bursting of gas bubbles at the surface of the magma. The compositions of fine silicate particles were found to vary between magmatic and nearly pure silica; this is consistent with depletion of metal ions by reactions in the acidic environment of the gas plume and vent. Measurements of the size, shape and composition of fine silicate particles may potentially offer insights into preemission, synemission, and postemission processes. The mass flux of fine silicate particles from Mt. Etna released during noneruptive volcanic degassing in 2004 and 2005 was estimated to be similar to 7000 kg d(-1). Analysis of particles in the range 0.1 < d/mu m < 100 by ion chromatography shows that there are persistent differences in the size distributions of sulfate aerosols between the two main summit plumes. Analysis of particles in the range 0.01 mu m < d < 0.1 mu m by scanning transmission electron microscopy (STEM) shows that there are significant levels of nanoparticles in the Mt. Etna plumes although their compositions remain uncertain.

Capacidade de enraizamento de variedades de nespereira submetidas à poda de renovação

O presente trabalho avaliou a capacidade de enraizamento de cinco variedades de nespereira (Eriobotrya japonica Lindl.), sendo Champagne, Precoce de Itaquera, Mizuho, Mogui e Tanaka, obtidas pela poda de renovação. Estacas tenras apicais, contendo um par de folhas e cerca de 15 cm, foram tratadas por cinco segundos com ácido indolbutírico (IBA) (0; 1.000; 3.000; 5.000 e 7.000 mg.L-1). O experimento foi conduzido em câmara de nebulização intermitente pertencente à UNESP/FCAV (21º15'22 S e 48º18'58 W). O delineamento experimental foi inteiramente casualizado, em esquema fatorial 5x5 (5 variedades e 5 concentrações de IBA), com 4 repetições e 10 estacas por parcela. As avaliações foram feitas após 90 dias. Os resultados indicaram um incremento de enraizamento e número de raízes crescente com a concentração de IBA utilizada, com exceção da variedade Mogui, que apresentou melhores resultados apenas quanto ao comprimento de raízes. Posterior ao transplantio, a sobrevivência das mudas foi alta (90%), apresentando condições de serem plantadas no campo, aos seis meses, ou de serem enxertadas aos oito meses, decorrido desde o estaqueamento.

A preliminary physicochemical, exergetic and economic study of hydrogen production utilizing glycerol

This work has as objective to demonstrate technical and economic viability of hydrogen production utilizing glycerol. The volume of this substance, which was initially produced by synthetic ways (from oil-derived products), has increased dramatically due mainly to biodiesel production through transesterification process which has glycerol as main residue. The surplus amount of glycerol has been generally utilized to feed poultry or as fuel in boilers, beyond other applications such as production of soaps, chemical products for food industry, explosives, and others. The difficulty to allocate this additional amount of glycerol has become it in an enormous environment problem, in contrary to the objective of biodiesel chain, which is to diminish environmental impact substituting oil and its derivatives, which release more emissions than biofuels, do not contribute to CO2-cycle and are not renewable sources. Beyond to utilize glycerol in combustion processes, this material could be utilized for hydrogen production. However, a small quantity of works (theoretical and experimental) and reports concerning this theme could be encountered. Firstly, the produced glycerol must be purified since non-reacted amounts of materials, inclusively catalysts, contribute to deactivate catalysts utilized in hydrogen production processes. The volume of non-reacted reactants and non-utilized catalysts during transesterification process could be reutilized. Various technologies of thermochemical generation of hydrogen that utilizes glycerol (and other fuels) were evaluated and the greatest performances and their conditions are encountered as soon as the most efficient technology of hydrogen production. Firstly, a physicochemical analysis must be performed. This step has as objective to evaluate the necessary amount of reactants to produce a determined volume of hydrogen and determine thermodynamic conditions (such as temperature and pressure) where the major performances of hydrogen production could be encountered. The calculations are based on the process where advance degrees are found and hence, fractions of products (especially hydrogen, however, CO2, CO, CH4 and solid carbon could be also encountered) are calculated. To produce 1 Nm3/h of gaseous hydrogen (necessary for a PEMFC - Proton Exchange Membrane Fuel Cell - containing an electric efficiency of about 40%, to generate 1 kWh), 0,558 kg/h of glycerol is necessary in global steam reforming, 0,978 kg/h of glycerol in partial oxidation and cracking processes, and 0,782 kg/h of glycerol in autothermal reforming process. The dry reforming process could not be performed to produce hydrogen utilizing glycerol, in contrary to the utilization of methane, ethanol, and other hydrocarbons. In this study, steam reforming process was preferred due mainly to higher efficiencies of production and the need of minor amount of glycerol as cited above. In the global steam reforming of glycerine, for one mole of glycerol, three moles of water are necessary to produce three moles of CO2 and seven moles of H2. The response reactions process was utilized to predict steam reforming process more accurately. In this mean, the production of solid carbon, CO, and CH4, beyond CO2 and hydrogen was predicted. However, traces of acetaldehyde (C2H2), ethylene (C2H4), ethylene glycol, acetone, and others were encountered in some experimental studies. The rates of determined products obviously depend on the adopted catalysts (and its physical and chemical properties) and thermodynamic conditions of hydrogen production. Eight reactions of steam reforming and cracking were predicted considering only the determined products. In the case of steam reforming at 600°C, the advance degree of this reactor could attain its maximum value, i.e., overall volume of reactants could be obtained whether this reaction is maintained at 1 atm. As soon as temperature of this reaction increases the advance degree also increase, in contrary to the pressure, where advance degree decrease as soon as pressure increase. The fact of temperature of reforming is relatively small, lower costs of installation could be attained, especially cheaper thermocouples and smaller amount of thermo insulators and materials for its assembling. Utilizing the response reactions process in steam reforming, the predicted volumes of products, for the production of 1 Nm3/h of H2 and thermodynamic conditions as cited previously, were 0,264 kg/h of CO (13% of molar fraction of reaction products), 0,038 kg/h of CH4 (3% of molar fraction), 0,028 kg/h of C (3% of molar fraction), and 0,623 kg/h of CO2 (20% of molar fraction). Through process of water-gas shift reactions (WGSR) an additional amount of hydrogen could be produced utilizing mainly the volumes of produced CO and CH4. The overall results (steam reforming plus WGSR) could be similar to global steam reforming. An attention must to be taking into account due to the possibility to produce an additional amount of CH4 (through methanation process) and solid carbon (through Boudouard process). The production of solid carbon must to be avoided because this reactant diminishes (filling the pores) and even deactivate active area of catalysts. To avoid solid carbon production, an additional amount of water is suggested. This method could be also utilized to diminish the volume of CO (through WGSR process) since this product is prejudicial for the activity of low temperature fuel cells (such as PEMFC). In some works, more three or even six moles of water are suggested. A net energy balance of studied hydrogen production processes (at 1 atm only) was developed. In this balance, low heat value of reactant and products and utilized energy for the process (heat supply) were cited. In the case of steam reforming utilizing response reactions, global steam reforming, and cracking processes, the maximum net energy was detected at 700°C. Partial oxidation and autothermal reforming obtained negative net energy in all cited temperatures despite to be exothermic reactions. For global steam reforming, the major value was 114 kJ/h. In the case of steam reforming, the highest value of net energy was detected in this temperature (-170 kJ/h). The major values were detected in the cracking process (up to 2586 kJ/h). The exergetic analysis has as objective, associated with physicochemical analysis, to determine conditions where reactions could be performed at higher efficiencies with lower losses. This study was performed through calculations of exergetic and rational efficiencies, and irreversibilities. In this analysis, as in the previously performed physicochemical analysis, conditions such as temperature of 600°C and pressure of 1 atm for global steam reforming process were suggested due to lower irreversibility and higher efficiencies. Subsequently, higher irreversibilities and lower efficiencies were detected in autothermal reforming, partial oxidation and cracking process. Comparing global reaction of steam reforming with more-accurate steam reforming, it was verified that efficiencies were diminished and irreversibilities were increased. These results could be altered with introduction of WGSR process. An economic analysis could be performed to evaluate the cost of generated hydrogen and determine means to diminish the costs. This analysis suggests an annual period of operation between 5000-7000 hours, interest rates of up to 20% per annum (considering Brazilian conditions), and pay-back of up to 20 years. Another considerations must to be take into account such as tariffs of utilized glycerol and electricity (to be utilized as heat source and (or) for own process as pumps, lamps, valves, and other devices), installation (estimated as US$ 15.000 for a plant of 1 Nm3/h) and maintenance cost. The adoption of emission trading schemes such as carbon credits could be performed since this is a process with potential of mitigates environment impact. Not considering credit carbons, the minor cost of calculated H2 was 0,16288 US$/kWh if glycerol is also utilized as heat sources and 0,17677 US$/kWh if electricity is utilized as heat sources. The range of considered tariff of glycerol was 0-0,1 US$/kWh (taking as basis LHV of H2) and the tariff of electricity is US$ 0,0867 US$/kWh, with demand cost of 12,49 US$/kW. The costs of electricity were obtained by Companhia Bandeirante, localized in São Paulo State. The differences among costs of hydrogen production utilizing glycerol and electricity as heat source was in a range between 0,3-5,8%. This technology in this moment is not mature. However, it allows the employment generation with the additional utilization of glycerol, especially with plants associated with biodiesel plants. The produced hydrogen and electricity could be utilized in own process, increasing its final performance.

Migración internacional y protección social

Incluye Bibliografía

Ação de óleos essenciais no controle de sigatoka-negra (Mycosphaerella fijiensis) Morelet de bananeiras (Musa sp)

Pós-graduação em Ciências Biológicas (Botânica) - IBB

A influência da aplicação de fluído de corte no torneamento da liga de aluminio AA 7075

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Anatomia da madeira de espécies de Cerrado sensu lato do Estado de São Paulo

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Propagação de espécies de Annonaceae com estacas caulinares

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Production and evaluation of recycled polymers from açaí fibers

The possibility of recycling and the favorable mechanical properties of the products have encouraged the study and production of thermoplastic composites from natural fibrous waste. Açaí (cabbage palm) fiber, which is removed from the seed, has been slightly investigated, as compared to what is already known about the fruit pulp. In this study, the influence of açaí fiber as an element of reinforcement in recycled everyday usage thermoplastics using simple, low cost methodology was evaluated. Recycled matrixes of high impact polystyrene and polypropylene were molded by hot compression from which the fiber composites were obtained. The FTIR technique showed that the process was efficient in preventing degradation of the açaí fibers. The influence of the fiber on the mechanical behavior of the recycled matrixes was investigated by microscopic images of compression and impact tests. The results showed better impact performance for the fiber combined with the polymeric matrixes.