Efeito da concentração de nitrogênio na solução nutritiva e do número de frutos por planta sobre a produção do meloeiro

O trabalho foi conduzido em casa de vegetação, na UNESP em Jaboticabal (SP), de junho a novembro de 2001, com o objetivo de avaliar a produção do melão (Cucumis melo var. reticulatus), híbrido Bônus nº2, cultivado em sistema hidropônico NFT, em função da concentração de nitrogênio na solução nutritiva (80, 140, 200 e 300 mg L-1) e número de frutos por planta (2, 3, 4 e livre). O delineamento experimental utilizado foi o de blocos ao acaso, em parcelas subdivididas, com seis repetições. Aos 80 dias após o transplantio, foram observados 2, 3, 4 e 5,1 frutos por planta e, posteriormente na colheita, 2, 2,9, 3,0 e 3,4 frutos por planta, respectivamente para os tratamentos com 2, 3, 4 e fixação livre, sendo esta redução atribuída ao abortamento de frutos. Houve redução no peso médio do 1º, 2º e 3º fruto colhido, com o aumento da concentração de nitrogênio. Plantas com o menor número de frutos, apresentaram maior peso médio dos mesmos, porém com menor produção por planta. A maior produção (2.474 g/planta) foi obtida com 80 mg L-1 de nitrogênio na solução nutritiva.

Desempenho de linhagens de melão rendilhado em casa de vegetação

Avaliaram-se 20 linhagens de melão rendilhado, obtidas em programa de melhoramento genético do meloeiro da UNESP, com relação às características associadas à produção e qualidade dos frutos. O experimento foi conduzido em casa de vegetação da UNESP em Jaboticabal, de junho de 2001 a dezembro de 2002. Utilizou-se o delineamento de blocos ao acaso com 20 tratamentos (linhagens), em quatro repetições. Cada parcela foi composta por oito plantas no espaçamento 0,5 x 1,0 m. Foram avaliados a produtividade (g/m²), peso médio, diâmetro transversal e longitudinal do lóculo e do fruto, índice de formato do fruto, espessura e coloração do mesocarpo e do epicarpo e teor de sólidos solúveis (ºBrix) dos frutos. As linhagens JAB-24-3, JAB-24-4, JAB-24-5, JAB-24-7, JAB-24-8, JAB-24-9, JAB-24-11, JAB-24-12, JAB-24-13, JAB-24-14, JAB-24-15, JAB-24-18 e JAB-24-20 se destacaram das demais na maioria das características avaliadas, demonstrando bom potencial para obtenção de híbridos comerciais.

Net melon resistance to Didymella bryoniae according to grafting and potassium levels

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Determinação experimental e modelagem termodinâmica do ponto de turbidez de sistemas aquosos com tensoativos nonilfenolpolietoxilados

The nonionic surfactants are composed of substances whose molecules in solution, does not ionize. The solubility of these surfactants in water due to the presence of functional groups that have strong affinity for water. When these surfactants are heated is the formation of two liquid phases, evidenced by the phenomenon of turbidity. This study was aimed to determine the experimental temperature and turbidity nonilfenolpoliethoxyled subsequently perform a thermodynamic modeling, considering the models of Flory-Huggins and the empirical solid-liquid equilibrium (SLE). The method used for determining the turbidity point was the visual method (Inoue et al., 2008). The experimental methodology consisted of preparing synthetic solutions of 0,25%, 0,5%, 1%, 2%, 3%, 4%, 5%, 6%, 7%, 8%, 9%, 10%, 12,5%, 15%, 17% and 20% by weight of surfactant. The nonionic surfactants used according to their degree of ethoxylation (9.5, 10, 11, 12 and 13). During the experiments the solutions were homogenized and the bath temperature was gradually increased while the turbidity of the solution temperature was checked visually Inoue et al. (2003). These temperature data of turbidity were used to feed the models evaluated and obtain thermodynamic parameters for systems of surfactants nonilfenolpoliethoxyled. Then the models can be used in phase separation processes, facilitating the extraction of organic solvents, therefore serve as quantitative and qualitative parameters. It was observed that the solidliquid equilibrium model (ESL) was best represented the experimental data.

Determinação de dados de equilíbrio líquido-vapor a altas pressões para sistemas de hidrocarbonetos assimétricos

Crude oil is a complex liquid mixture of organic and inorganic compounds that are dominated by hydrocarbons. It is a mixture of alkanes from the simplest to more complex aromatic compounds that are present derivatives such as gasoline, diesel, alcohol, kerosene, naphtha, etc.. These derivatives are extracted from any oil, however, only with a very high quality, in other words, when the content of hydrocarbons of low molecular weight is high means that production of these compounds is feasible. The American Petroleum Institute (API) developed a classification system for the various types of oil. In Brazil, the quality of most of the oil taken from wells is very low, so it is necessary to generate new technology to develop best practices for refining in order to produce petroleum products of higher commercial value. Therefore, it is necessary to study the thermodynamic equilibrium properties of its derivative compounds of interest. This dissertation aims to determine vapor-liquid equilibrium (VLE) data for the systems Phenilcyclohexane - CO2, and Cyclohexane - Phenilcyclohexane - CO2 at high pressure and temperatures between 30 to 70oC. Furthermore, comparisons between measured VLE experimental data from this work and from the literature in relation to the Peng- Robinson molecular thermodynamic model, using a simulation program SPECS IVCSEP v5.60 and two adjustable interaction parameters, have been performed for modeling and simulation purposes. Finally, the developed apparatus for determination of phase equilibrium data at high pressures is presented

Modelagem e simulação da deposição de parafinas em escoamento turbulento

The flow assurance has become one of the topics of greatest interest in the oil industry, mainly due to production and transportation of oil in regions with extreme temperature and pressure. In these operations the wax deposition is a commonly problem in flow of paraffinic oils, causing the rising costs of the process, due to increased energy cost of pumping, decreased production, increased pressure on the line and risk of blockage of the pipeline. In order to describe the behavior of the wax deposition phenomena in turbulent flow of paraffinic oils, under different operations conditions, in this work we developed a simulator with easy interface. For that we divided de work in four steps: (i) properties estimation (physical, thermals, of transport and thermodynamics) of n-alkanes and paraffinic mixtures by using correlations; (ii) obtainment of the solubility curve and determination the wax appearance temperature, by calculating the solid-liquid equilibrium of parafinnic systems; (iii) modelling wax deposition process, comprising momentum, mass and heat transfer; (iv) development of graphic interface in MATLAB® environment for to allow the understanding of simulation in different flow conditions as well as understand the matter of the variables (inlet temperature, external temperature, wax appearance temperature, oil composition, and time) on the behavior of the deposition process. The results showed that the simulator developed, called DepoSim, is able to calculate the profile of temperature, thickness of the deposit, and the amount of wax deposited in a simple and fast way, and also with consistent results and applicable to the operation

Estudo do equilíbrio líquido-vapor do sistema água+etanol+líquido iônico visando a separação do álcool anidro

Anhydrous ethanol is used in chemical, pharmaceutical and fuel industries. However, current processes for obtaining it involve high cost, high energy demand and use of toxic and pollutant solvents. This problem occurs due to the formation of an azeotropic mixture of ethanol + water, which does not allow the complete separation by conventional methods such as simple distillation. As an alternative to currently used processes, this study proposes the use of ionic liquids as solvents in extractive distillation. These are organic salts which are liquids at low temperatures (under 373,15 K). They exhibit characteristics such as low volatility (almost zero/ low vapor ), thermal stability and low corrosiveness, which make them interesting for applications such as catalysts and as entrainers. In this work, experimental data for the vapor pressure of pure ethanol and water in the pressure range of 20 to 101 kPa were obtained as well as for vapor-liquid equilibrium (VLE) of the system ethanol + water at atmospheric pressure; and equilibrium data of ethanol + water + 2-HDEAA (2- hydroxydiethanolamine acetate) at strategic points in the diagram. The device used for these experiments was the Fischer ebulliometer, together with density measurements to determine phase compositions. The experimental data were consistent with literature data and presented thermodynamic consistency, thus the methodology was properly validated. The results were favorable, with the increase of ethanol concentration in the vapor phase, but the increase was not shown to be pronounced. The predictive model COSMO-SAC (COnductor-like Screening MOdels Segment Activity Coefficient) proposed by Lin & Sandler (2002) was studied for calculations to predict vapor-liquid equilibrium of systems ethanol + water + ionic liquids at atmospheric pressure. This is an alternative for predicting phase equilibrium, especially for substances of recent interest, such as ionic liquids. This is so because no experimental data nor any parameters of functional groups (as in the UNIFAC method) are needed

Determinação de dados de equilíbrio de fases para sistemas aquosos com eletrólitos

In the present work are established initially the fundamental relationships of thermodynamics that govern the equilibrium between phases, the models used for the description of the behavior non ideal of the liquid and vapor phases in conditions of low pressures. This work seeks the determination of vapor-liquid equilibrium (VLE) data for a series of multicomponents mixtures of saturated aliphatic hydrocarbons, prepared synthetically starting from substances with analytical degree and the development of a new dynamic cell with circulation of the vapor phase. The apparatus and experimental procedures developed are described and applied for the determination of VLE data. VLE isobarics data were obtained through a Fischer s ebulliometer of circulation of both phases, for the systems pentane + dodecane, heptane + dodecane and decane + dodecane. Using the two new dynamic cells especially projected, of easy operation and low cost, with circulation of the vapor phase, data for the systems heptane + decane + dodecane, acetone + water, tween 20 + dodecane, phenol + water and distillation curves of a gasoline without addictive were measured. Compositions of the equilibrium phases were found by densimetry, chromatography, and total organic carbon analyzer. Calibration curves of density versus composition were prepared from synthetic mixtures and the behavior excess volumes were evaluated. The VLE data obtained experimentally for the hydrocarbon and aqueous systems were submitted to the test of thermodynamic consistency, as well as the obtained from the literature data for another binary systems, mainly in the bank DDB (Dortmund Data Bank), where the Gibbs-Duhem equation is used obtaining a satisfactory data base. The results of the thermodynamic consistency tests for the binary and ternary systems were evaluated in terms of deviations for applications such as model development. Later, those groups of data (tested and approved) were used in the KijPoly program for the determination of the binary kij parameters of the cubic equations of state original Peng-Robinson and with the expanded alpha function. These obtained parameters can be applied for simulation of the reservoirs petroleum conditions and of the several distillation processes found in the petrochemistry industry, through simulators. The two designed dynamic cells used equipments of national technology for the determination of VLE data were well succeed, demonstrating efficiency and low cost. Multicomponents systems, mixtures of components of different molecular weights and also diluted solutions may be studied in these developed VLE cells

Síntese e caracterização de tensoativos e estudo de equilíbrio de fase dos sistemas CnH2n+2/H2O/CnH2n+1COONa/But-OH

The growing utilization of surfactants in several different areas of industry has led to an increase on the studies involving solutions containing this type of molecules. Due to its amphiphilic nature, its molecule presents one polar part and one nonpolar end, which easily interacts with other molecules, being able to modify the media properties. When the concentration in which its monomers are saturated, the airliquid system interface is reached, causing a decrease in interfacial tension. The surfactants from pure fatty acids containing C8, C12 and C16 carbonic chains were synthesized in an alcoholic media using sodium hydroxide. They were characterized via thermal analysis (DTA and DTG) and via infrared spectroscopy, with the intention of observing their purity. Physical and chemical properties such as superficial tension, critical micelle concentration (c.m.c), surfactant excess on surface and Gibbs free energy of micellization were determined in order to understand the behaviour of these molecules with an aqueous media. Pseudo-ternary phase diagrams were obtained aiming to limit the Windsor equilibria conditions so it could be possible to understand how the surfactants carbonic chain size contributes to the microemulsion region. Solutions with known concentrations were prepared to study how the surfactants can influence the dynamic light scattering spectroscopy (DLS) and how the diffusion coefficient is influenced when the media concentration is altered. The results showed the variation on the chain size of the studied surfactant lipophilic part allows the conception of surfactants with similar interfacial properties, but dependent on the size of the lipophilic part of the surfactant. This variation causes the surfactant to have less tendency of microemulsionate oil in water. Another observed result is that the n-alcanes molecule size promoted a decrease on the microemulsion region on the obtained phase diagrams

Determinação de Dados de Equilíbrio Líquido-Vapor para Sistemas Hidrocarbonetos e Desenvolvimento de uma Nova Célula Dinâmica

In the present work are established initially the fundamental relationships of thermodynamics that govern the equilibrium between phases, the models used for the description of the behavior non ideal of the liquid and vapor phases in conditions of low pressures. This work seeks the determination of vapor-liquid equilibrium (VLE) data for a series of multicomponents mixtures of saturated aliphatic hydrocarbons, prepared synthetically starting from substances with analytical degree and the development of a new dynamic cell with circulation of the vapor phase. The apparatus and experimental procedures developed are described and applied for the determination of VLE data. VLE isobarics data were obtained through a Fischer's ebulliometer of circulation of both phases, for the systems pentane + dodecane, heptane + dodecane and decane + dodecane. Using the two new dynamic cells especially projected, of easy operation and low cost, with circulation of the vapor phase, data for the systems heptane + decane + dodecane, acetone + water, tween 20 + dodecane, phenol + water and distillation curves of a gasoline without addictive were measured. Compositions of the equilibrium phases were found by densimetry, chromatography, and total organic carbon analyzer. Calibration curves of density versus composition were prepared from synthetic mixtures and the behavior excess volumes were evaluated. The VLE data obtained experimentally for the hydrocarbon and aqueous systems were submitted to the test of thermodynamic consistency, as well as the obtained from the literature data for another binary systems, mainly in the bank DDB (Dortmund Data Bank), where the Gibbs-Duhem equation is used obtaining a satisfactory data base. The results of the thermodynamic consistency tests for the binary and ternary systems were evaluated in terms of deviations for applications such as model development. Later, those groups of data (tested and approved) were used in the KijPoly program for the determination of the binary kij parameters of the cubic equations of state original Peng-Robinson and with the expanded alpha function. These obtained parameters can be applied for simulation of the reservoirs petroleum conditions and of the several distillation processes found in the petrochemistry industry, through simulators. The two designed dynamic cells used equipments of national technology for the determination Humberto Neves Maia de Oliveira Tese de Doutorado PPGEQ/PRH-ANP 14/UFRN of VLE data were well succeed, demonstrating efficiency and low cost. Multicomponents systems, mixtures of components of different molecular weights and also diluted solutions may be studied in these developed VLE cells

Avaliação oxidativa do biodiesel de pinhão manso em diferentes processos de purificação

The objective of this study was to analyze the oxidative stability of biodiesel from jatropha obtained from different purification processes, three wet processes with different drying (in a vacuum oven, conventional oven and in anhydrous sodium sulfate) and dry (purification with magnesium silicate adsorbent). Raw materials of different qualities (jatropha crop ancient and recent crop) were used. The Jatropha oil was extracted by mechanical extraction and refined. The Jatropha biodiesel was obtained by the transesterification reaction in ethyl route using alkaline catalysis. The biodiesel samples were characterized by analysis of water content, carbon residue, Absorption Spectroscopy in the Infrared Region and Thermogravimetry. Thermogravimetric curves of purified PUsv* PUsq* and had higher initial decomposition temperatures, indicating that the most stable, followed by samples PU* and PUSC*. Besides the sample SP* is a smaller initial temperature, confirming the sample without purification to be less thermally stable. The percentage mass loss of the purified samples showed conversion of about 98.5%. The results of analyzes carbon residue and infrared suggested that contamination by impurities is the main factor for decreased oxidative stability of biodiesel. The oxidative stability was assessed from periodic monitoring, using the techniques of Rancimat, peroxide index, acid value and Pressurized Differential Scanning Calorimetry. Samples of biodiesel from jatropha which showed better oxidative stability were of the best quality raw material and wet scrubbing: PUsq* with dry chemical, using anhydrous sodium sulfate and PUsv* with vacuum drying, which had oxidative stability 6 hours in Rancimat time 0 days, within the limits established by the Technical Regulation No. 4/2012 of the ANP, without the addition of antioxidant, suggesting that these procedures the least influence on the oxidative stability of biodiesel

Condução de melão rendilhado sob cultivo protegido

Estudou-se o comportamento de dois híbridos de melão rendilhado (Bônus nº 2 - polpa verde e D. Carlos - polpa salmão), conduzidos com uma ou duas hastes, em três diferentes posições de fixação dos frutos (5º ao 8º, 9º ao 11º e 12º ao 15º nó). Adotou-se delineamento de blocos ao acaso, com três repetições, no esquema fatorial 2 X 2 X 3. O experimento foi conduzido no segundo semestre de 1998, em região de clima Cwa. Realizou-se plantio em fileira única, com espaçamento de 1,25 m entre linhas e 0,25 m entre plantas, com irrigação por gotejamento, em casa de vegetação tipo arco, com laterais abertas, sendo as plantas conduzidas alternadamente uma para cada lado, em forma de V; adotou-se o limite de dois frutos por planta. Ocorreram interações entre híbridos e posições de fixação do fruto para altura de fixação do fruto, entre híbrido e sistema de condução para conteúdo de sólidos solúveis, entre sistema de condução e posição de fixação do fruto para número médio de frutos por planta e produção total de frutos por planta. Plantas conduzidas com duas hastes apresentaram maior distância entre o solo e o nó de fixação do fruto (55,17 cm), em relação às com uma haste (39,50 cm) para os dois híbridos. O híbrido Bônus nº 2 apresentou maior quantidade de matéria seca por planta, na floração (22,61 g) e na colheita (74,34 g), maior área foliar por planta, na floração (0,3613 m²) e colheita (0,7701 m²), maior número de frutos por planta (1,15), maior produção total de frutos por planta (1,18 kg), e maior conteúdo de sólidos solúveis (15,0%) em relação a 'D. Carlos' (16,39 g, 52,48 g, 0,2550 m², 0,6094 m², 0,78 frutos, 0,848 kg/fruto, e 11,3%, respectivamente). O híbrido D. Carlos, conduzido com duas hastes, apresentou maior conteúdo de sólidos solúveis (12,0%) em relação a uma haste (10,5%), o que não foi observado para 'Bônus nº 2'. A posição de fixação do fruto não influenciou no conteúdo de sólidos solúveis (12,9 a 13,3%), na massa média do fruto (1,050 a 1,090 kg) e no número médio de frutos por planta (1,05 a 1,30). Entretanto, para a produção total por planta, no sistema de condução com uma ou duas hastes, as posições acima do 9º nó até o 15º nó apresentaram maior produção (1,123 a 1,352 kg/planta). 'D. Carlos' mostrou-se mais precoce (81 dias em média) em relação a 'Bônus nº 2' (98 dias em média).

Características de cultivares de melão rendilhado cultivadas em casa de vegetação

Este trabalho teve como objetivo avaliar cinco cultivares de melão rendilhado com relação as características associadas à produção e qualidade dos frutos e quanto à aparência. O experimento foi conduzido em casa de vegetação da Faculdade de Ciências Agrárias e Veterinárias-UNESP, Câmpus de Jaboticabal. Utilizou-se o delineamento em blocos ao acaso com 5 tratamentos compostos pelas cultivares Sunrise; Aragon; Halest Best Jumbo; Nero e Bônus nº 2 e 4 repetições. Foram avaliados o peso médio dos frutos comercializáveis; diâmetro e comprimento médio de frutos; espessura média e coloração do mesocarpo e epicarpo; teor de sólidos solúveis (ºBrix), pH e acidez total. O híbrido Bônus nº 2 destacou-se com relação à produção média/m², peso médio dos frutos (Kg), espessura da polpa (cm) e ºBrix, características importantes para a produção e comercialização dos frutos de meloeiro, podendo ser indicado para cultivo em casa de vegetação.

Divergência genética entre cinco genótipos de melão rendilhado

Estimou-se a divergência genética entre cinco genótipos de melão rendilhado (Cucumis melo var. reticulatus Naud.) (JAB-20, JAB-21, JAB-22, JAB-23 e 'Bônus nº 2') e determinou-se qual a contribuição relativa das 16 características avaliadas [nº médio de flores masculinas, hermafroditas/planta; produção total de frutos/m², peso médio dos frutos comerciáveis; diâmetro médio transversal e longitudinal do fruto (DMTF e DMLF); diâmetro médio transversal da inserção do pedúculo (DMTP); espessura média do mesocarpo e epicarpo (EMM e EME); diâmetro médio longitudinal e transversal do lóculo (DMTL e DMLL); proporção da cavidade (PC); desprendimento de sementes (DS); teor de sólidos solúveis totais (SST), pH e acidez titulável (AT)] na divergência genética. Obtiveram-se dois grupos de similaridade: I- JAB-20, JAB-21 e 'Bônus nº2' e II- JAB-22 e JAB-23. As características DMLF, DMTP, DMLL, DS e SST foram as que mais contribuíram para a divergência genética entre os genótipos.

Ação de acibenzolar-s-methyl (BTH) isolado e em combinação com fungicidas no controle do cancro da haste em melão rendilhado

Determinou-se as melhores épocas de aplicação e dosagens do BTH e seu efeito no controle do cancro da haste isoladamente ou em combinação com fungicidas. Foram testadas duas doses de BTH (2,5 e 5,0 g/100L) aplicadas aos 11; 18; 22 e 24 dias após transplantio das mudas. Utilizou-se o delineamento inteiramente casualizado, no esquema fatorial 2 x 4 (doses x épocas) com oito repetições. Posteriormente, utilizou-se a melhor época e dose de BTH associada aos fungicidas: difenoconazole (30 mL de p.c./100L), azoxystrobin (16 mL de p.c./100L) alternado com chlorothalonil (250 g de p.c./100L) e chlorothalonil (250 g de p.c./100L). Utilizou-se também BTH isoladamente e benomyl (70 g de p.c./100L) sem a adição de BTH. As aplicações foram realizadas em intervalos de sete dias até os 28 dias após o transplantio. Os seis tratamentos foram distribuídos inteiramente ao acaso em 15 repetições. Avaliou-se a severidade da doença por meio de escala de notas. Os resultados encontrados demonstraram que a associação de difenoconazole + BTH foi mais eficiente no controle do cancro da haste em melão rendilhado.