Adubação orgânica na produção e qualidade de frutos de maracujá-doce

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

Distribuição do sistema radicular do maracujazeiro-doce cultivado com adubação química e orgânica

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.

Cultivo de bananas em diferentes áreas na ilha de Tenerife

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

Preservação de fungos fitopatogênicos habitantes do solo

A preservação de fungos fitopatogênicos por longos períodos de tempo é importante para que pesquisas possam ser realizadas a qualquer momento. Os fungos habitantes do solo são organismos que podem produzir estruturas de resistência em face de situações adversas, tais como ausência de hospedeiros e ou condições climáticas desfavoráveis para a sua sobrevivência. O objetivo deste trabalho foi desenvolver metodologias de preservação de estruturas de resistência para os fungos Fusarium oxysporum f.sp. lycopersici raça 2, Macrophomina phaseolina, Rhizoctonia solani AG4 HGI, Sclerotium rolfsii, Sclerotinia sclerotiorum e Verticillium dahliae. O delineamento foi inteiramente casualizado, com um método de produção de estruturas para cada fungo, submetido a três tratamentos [temperatura ambiente de laboratório (28±2ºC), de geladeira (5ºC) e de freezer (-20ºC)] e com dois frascos por temperatura. Mensalmente, e por um período de um ano, a sobrevivência e o vigor das colônias de cada patógeno foram avaliadas em meios de cultura específicos. Testes de patogenicidade foram realizados após um ano de preservação, com as estruturas que sobreviveram aos melhores tratamentos (temperatura) para todos os fungos. As melhores temperaturas (tratamentos) para preservar os fungos foram: a) F. oxysporum f.sp. lycopersici em temperatura de refrigeração e de freezer (5,2 e 2,9 x 10³ufc.g-1 de talco, respectivamente); b) M. phaseolina em temperatura de refrigeração [100% de sobrevivência (S) e índice 3 de vigor (V)] e S. rolfsii em temperatura ambiente (74,4% S e 1 V) e c) S. sclerotiorum e V. dahliae, ambos em temperatura de freezer (100% S e 3 V). Após um ano de preservação, somente V. dahliae perdeu a patogenicidade na metodologia desenvolvida.

Avaliação da degradação de macrófitas aquáticas descartadas em ambiente protegido

Com o intuito de buscar informações sobre a degradação de macrófitas aquáticas descartadas em pilhas, após ações do controle mecânico, foi conduzido um experimento no Departamento de Recursos Naturais - Ciências Ambientais, UNESP, campus de Botucatu-SP. Para atender o objetivo proposto, foram montadas pilhas com volume de 2,25 m³, compostas, principalmente, por três espécies de macrófitas, retiradas do reservatório da UHE Americana/SP. Foram coletadas amostras na montagem das pilhas, aos 15, 30, 60 e 90 dias, para o acompanhamento da temperatura da pilha e do pH do material orgânico durante o processo, além de uma análise química do composto ao final dos 90 dias. Os tratamentos foram: T1 - somente plantas aquáticas e revolvimento da pilha a cada sete dias; T2 - somente plantas aquáticas e revolvimento a cada quatro dias; T3 - plantas aquáticas + permagel, com revolvimento a cada sete dias; e T4 - plantas aquáticas + permagel e revolvimento a cada quatro dias. Utilizou-se o delineamento estatístico inteiramente casualizado, sendo a análise estatística realizada para coleta aos 90 dias, empregando o programa SISVAR. Concluiu-se que os resultados de macro e micronutrientes, temperatura, umidade, pH, relação C/N e redução do volume das pilhas foram semelhantes aos observados quando se procedeu ao descarte em pilhas com volume de 4,5 m³ sobre o solo.

Fermentação alcoólica utilizando líquido da casca de coco verde como fonte de nutrientes

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

Extração do óleo e caracterização dos resíduos da borra de petróleo para fins de reuso

The petroleum industry, in consequence of an intense activity of exploration and production, is responsible by great part of the generation of residues, which are considered toxic and pollutants to the environment. Among these, the oil sludge is found produced during the production, transportation and refine phases. This work had the purpose to develop a process to recovery the oil present in oil sludge, in order to use the recovered oil as fuel or return it to the refining plant. From the preliminary tests, were identified the most important independent variables, like: temperature, contact time, solvents and acid volumes. Initially, a series of parameters to characterize the oil sludge was determined to characterize its. A special extractor was projected to work with oily waste. Two experimental designs were applied: fractional factorial and Doehlert. The tests were carried out in batch process to the conditions of the experimental designs applied. The efficiency obtained in the oil extraction process was 70%, in average. Oil sludge is composed of 36,2% of oil, 16,8% of ash, 40% of water and 7% of volatile constituents. However, the statistical analysis showed that the quadratic model was not well fitted to the process with a relative low determination coefficient (60,6%). This occurred due to the complexity of the oil sludge. To obtain a model able to represent the experiments, the mathematical model was used, the so called artificial neural networks (RNA), which was generated, initially, with 2, 4, 5, 6, 7 and 8 neurons in the hidden layer, 64 experimental results and 10000 presentations (interactions). Lesser dispersions were verified between the experimental and calculated values using 4 neurons, regarding the proportion of experimental points and estimated parameters. The analysis of the average deviations of the test divided by the respective training showed up that 2150 presentations resulted in the best value parameters. For the new model, the determination coefficient was 87,5%, which is quite satisfactory for the studied system

Aperfeiçoamento no projeto de um protótipo de misturador-decantador à inversão de fases visando aplicação na indústria do petróleo

In the oil industry the mixture oil/water occurs in the operations of production, transportation and refining, as well as during the use of its derivatives. The amount of water produced associated with the oil varies and can reach values of 90% in volume in the case of mature phase of the production fields. The present work deals with the development of new design of the Mixer Settler based on Phase Inversion (MDIF) in a laboratory scale. We envisage this application in industrial scale so the phases of project, construction and operation are considered. The modifications most significant, in comparison with the original prototype, include the materials of construction and the substitution of the equipment used in the mixing stage of the process. It was tested the viability of substitution of the original system of mechanical mixing by a static mixer. A statistical treatment by means of an experimental design of composed central type was used in order to evaluate the behavior of the main variables of the separation process as function of the efficiency of separation for the new device. This procedure is useful to delimit an optimal region of operation with the equipment. The variables of process considered on the experimental design were: oil concentration in the feeding water (mg/L); Total volumetric flow rate (L/h); Ratio organic/water on volumetric basis (O/A). The separation efficiency is calculated by comparison of the content of oil and greases in the inlet and outlet of the equipment. For determination of TOG (Total Oil and Grease), the method used was based in the absorption of radiation in the infra-red region. The equipment used for these determinations was InfraCal® TOG/TPH Model HATR-T2 of the Wilks Enterprise, Incorporation. It´s important to stand out that this method of measure has being used by PETROBRAS S.A. Results of global efficiency of separation oil/water varied from 75.3 to 97.7% for contaminated waters containing up to 1664,1 mg/L of oil. By means of tests carried out with a real sample of contaminated water supplied by PETROBRAS we have got an effluent specified in terms of the legal standards required for discharging. Thus, the new design of equipment constitutes a real alternative for the conventional systems of treatment of produced water in the oil industry

Formação do pomar de tangerina 'Poncã', em função da adubação química e orgânica

Avaliou-se o efeito do esterco de curral curtido na adubação de formação do pomar de tangerineira 'Poncã' (Citrus reticulata, Blanco), comparando com a adubação química convencional. O experimento foi conduzido na Fazenda Experimental São Manuel da Faculdade de Ciências Agronômicas da UNESP, Câmpus de Botucatu-SP. Os tratamentos foram aplicados na adubação de formação do pomar durante dois anos. No primeiro ano, utilizaram-se 7,5; 15,0; 22,5 e 30,0 kg planta-1 de esterco de curral curtido e 400 g planta-1 de sulfato de amônio. Na adubação de formação do segundo ano, as doses de esterco de curral foram 15,0; 22,5; 30,0 e 37,5 kg planta-1 e 800 g planta-1 de sulfato de amônio. Nos dois anos, a adubação foi parcelada em três aplicações. Realizaram-se as avaliações aos 30; 150 e 270 dias após a última parcela de adubação do segundo ano, determinando-se: altura da planta, diâmetro do caule, volume, projeção e circunferência da copa. O delineamento experimental foi inteiramente casualizado, em parcelas subdivididas no tempo, e 3 repetições, sendo as parcelas representadas pela adubação e as subparcelas pelas épocas de avaliação. Verificou-se que, na média das avaliações, houve aumento linear das características avaliadas com o incremento das doses de esterco de curral curtido. Não houve diferença significativa entre os tratamentos com adubo orgânico e químico.

Microrganismos do solo produtores de fosfatases em diferentes sistemas agrícolas

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

Produção de fitomassa, teor e produtividade do óleo essencial de Baccharis dracunculifolia DC. em função da adubação orgânica

Objetivou-se avaliar a produção de fitomassa, teor e produtividade do óleo essencial de Baccharis dracuculifolia DC., em função de doses de adubo orgânico, e foram utilizadas mudas produzidas por semente, e mantidas sob sombrite pelo período de 84 dias até serem transplantadas para o campo, no espaçamento de 1,0 x 1,0 m, com irrigação por gotejamento. O delineamento estatístico utilizado foi em blocos ao acaso, com quatro repetições, e as doses de composto orgânico foram: 0, 10, 20, 30, 40 e 50 t ha-1. Foi realizada uma colheita, aos 150 dias após o transplante das mudas. O óleo essencial foi extraído por hidrodestilação e analisado em cromatógrafo a gás acoplado a espectrômetro de massas (Shimadzu, QP-5000). Todos os resultados foram submetidos à análise de variância pelo teste F seguido da análise de regressão e o teste Tukey para os dados: massa seca útil da parte aérea, teor e produtividade do óleo essencial. Para as variáveis massa seca total e massa seca útil da parte aérea, as dosagens estudadas influenciaram as plantas, que apresentaram os melhores resultados na dose 50 t ha-1. Para teor de óleo não houve influência significativa para as dosagens estudadas, porém a dose 30 t ha-1 apresentou o melhor resultado. Entretanto para a produtividade do óleo essencial, as dosagens estudadas influenciaram as plantas, que na dosagem 30 t ha-1 obtiveram os melhores resultados.

Desenvolvimento de um reator fotoquímico aplicável no tratamento de efluentes fenólicos presentes na indústria do petróleo

With water pollution increment at the last years, so many progresses in researches about treatment of contaminated waters have been developed. In wastewaters containing highly toxic organic compounds, which the biological treatment cannot be applied, the Advanced Oxidation Processes (AOP) is an alternative for degradation of nonbiodegradable and toxic organic substances, because theses processes are generation of hydroxyl radical based on, a highly reactivate substance, with ability to degradate practically all classes of organic compounds. In general, the AOP request use of special ultraviolet (UV) lamps into the reactors. These lamps present a high electric power demand, consisting one of the largest problems for the application of these processes in industrial scale. This work involves the development of a new photochemistry reactor composed of 12 low cost black light fluorescent lamps (SYLVANIA, black light, 40 W) as UV radiation source. The studied process was the photo-Fenton system, a combination of ferrous ions, hydrogen peroxide, and UV radiation, it has been employed for the degradation of a synthetic wastewater containing phenol as pollutant model, one of the main pollutants in the petroleum industry. Preliminary experiments were carrier on to estimate operational conditions of the reactor, besides the effects of the intensity of radiation source and lamp distribution into the reactor. Samples were collected during the experiments and analyzed for determining to dissolved organic carbon (DOC) content, using a TOC analyzer Shimadzu 5000A. The High Performance Liquid Chromatography (HPLC) was also used for identification of the cathecol and hydroquinone formed during the degradation process of the phenol. The actinometry indicated 9,06⋅1018 foton⋅s-1 of photons flow, for 12 actived lamps. A factorial experimental design was elaborated which it was possible to evaluate the influence of the reactants concentration (Fe2+ and H2O2) and to determine the most favorable experimental conditions ([Fe2+] = 1,6 mM and [H2O2] = 150,5 mM). It was verified the increase of ferrous ions concentration is favorable to process until reaching a limit when the increase of ferrous ions presents a negative effect. The H2O2 exhibited a positive effect, however, in high concentrations, reaching a maximum ratio degradation. The mathematical modeling of the process was accomplished using the artificial neural network technique

Degradação fotoquímica de hidrocarbonetos da gasolina em efluentes aquosos

Photo-oxidation processes of toxic organic compounds have been widely studied. This work seeks the application of the photo-Fenton process for the degradation of hydrocarbons in water. The gasoline found in the refinery, without additives and alcohol, was used as the model pollutant. The effects of the concentration of the following substances have been properly evaluated: hydrogen peroxide (100-200 mM), iron ions (0.5-1 mM) and sodium chloride (200 2000 ppm). The experiments were accomplished in reactor with UV lamp and in a falling film solar reactor. The photo-oxidation process was monitored by measurements of the absorption spectra, total organic carbon (TOC) and chemical oxygen demand (COD). Experimental results demonstrated that the photo-Fenton process is feasible for the treatment of wastewaters containing aliphatic hydrocarbons, inclusive in the presence of salts. These conditions are similar to the water produced by the petroleum fields, generated in the extraction and production of petroleum. A neural network model of process correlated well the observed data for the photooxidation process of hydrocarbons

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

Tratamento de materiais contaminados com bifenilas policloradas (PCBS) via extração convencional e fluído supercrítico

The decontamination of the materials has been subject of some studies. One of the factors that it increases the pollution is the lack of responsibility in the discarding of toxic trash, as for example the presence of PCB (Polychlorinated Biphenyls) in the environment. In the Brazilian regulations, the material contaminated with PCB in concentrations higher than 50 ppm must be stored in special places or destroyed, usually by incineration in plasma furnace with dual steps. Due to high cost of the procedure, new methodologies of PCBs removal has been studied. The objective of this study was to develop an experimental methodology and analytical methodology for quantification of removal of PCBs through out the processes of extractions using supercritical fluid and Soxhlet method, also technical efficiency of the two processes of extraction, in the treatment of contaminated materials with PCBs. The materials studied were soils and wood, both were simulated contamination with concentration of 6.000, 33.000 and 60.000 mg of PCB/ kg of materials. Soxhlet extractions were performed using 100 ml of hexane, and temperature of 180 ºC. Extractions by fluid supercritical were performed at conditions of 200 bar, 70°C, and supercritical CO2 flow-rate of 3 g/min for 1-3 hours. The extracts obtained were quantified using Gas chromatography-mass spectrometry (GC/MS). The conventional extractions were made according to factorial experimental planning technique 22, with aim of study the influence of two variables of process extraction for the Soxhlet method: contaminant concentration and extraction time for obtain a maximum removal of PCB in the materials. The extractions for Soxhlet method were efficient for extraction of PCBs in soil and wood in both solvent studied (hexane and ethanol). In the experimental extraction in soils, the better efficient of removal of PCBs using ethanol as solvent was 81.3% than 95% for the extraction using hexane as solvent, for equal time of extraction. The results of the extraction with wood showed statistically it that there is not difference between the extractions in both solvent studied. The supercritical fluid extraction in the conditions studied showed better efficiency in the extraction of PCBs in the wood matrix than in soil, for two hours extractions the obtain percentual of 43.9 ± 0.5 % for the total of PCBs extracted in the soils against 95.1 ± 0,5% for the total of PCBs extracted in the wood. The results demonstrated that the extractions were satisfactory for both technical studied