660 resultados para Nonionic surfactants
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The fat acid esters and tocopherolic derivatives are of great economic interest in many industries. The sunflower oil, which had its rich constitution in these composites, is a very interesting raw material source for the job in some sectors as bio-carburants, bio-lubrificants, bio-surfactants, dispersing agents, food industries, medicines and cosmetics. A system emulsified steady from this oil can wide be used in the therapeutical one, therefore it is of easy acceptance for the patient, for being pharmaceutical forms that allow a better medicine administration. The chemical composition characteristics, rich in unsaturad fat acid and tocopherolic derivatives, the sunflower oil, make of the emulsified systems contend this oil a proposal promising for formularizations of pharmaceutical and cosmetic use with antirust and photoprotection. The general objective of this work was to apply the HLB beddings to determine the sunflower oil critical HLB and, from this, to be able to evaluate the ideal mixture of the constituent of this system through the study of the ternary diagrams for the determination of the ratio of constituent that will generate the emulsion most steady
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Praziquantel (PRZ) is the main drug used for treatment of schistosomiasis in Brazil. It is administered by oral rout as tablets. However, has low aqueous solubility which limits this therapeutic success dosage form and availability of liquid forms. The emulsion systems have great potential and represent an interesting strategy to increase the solubility of drugs. The aim of study was the development and characterization of lipid-emulsified liquid systems of the type oil in water (O / W), the base of soybean oil as the internal phase stabilized by surfactants pair Tween® 80 and Span® 80, for improving the phase biopharmaceutical of PRZ. After selecting the best value of Hydrophilic-Lipophilic Balance (HLB = 11), the parameters of the preparation of the formulations were optimized emulsification technique. The emulsions were successfully obtained; the liquid forms provided exhibited Newtonian behavior and an increase in solubility of PRZ higher than 20 times. The accelerated stability study demonstrated the stability of the emulsions and the effect of cosurfactants investigated. The study of the dynamics of interaction between components in the diagram showed pseudoternary phase regions to obtain O/W emulsions, whereas the study of the interaction of the components and their effect on system structure and the efficiency of incorporation of the drug led to systems with an amount of soluble drug even higher (about 1.5%), which demonstrates the potential of this new input mainly for the treatment of schistosomiasis, which resulted in the filing of patent BR 10 2013 0004 55 3
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The selectivity of the herbicide flazasulfaron was evaluated when applied at two rates (50 and 100 g/ha) with and without surfactants (Aterbane or Agral at 0.2% v/v). The treatment was applied at early (three leaves) and late (five to six leaves) stages of the postemergence of sugarcane plants (var. RB845257) grown in two soils (sandy and clay) with good moisture status before and after application. Despite the toxicity symptoms, especially at the late stage with the higher rate of application in the sandy soil, the herbicide did not affect the growth nor the stalk yield. The presence of the surfactants had no effect on the toxicity symptoms.
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Com o objetivo de estudar a influência do momento da chuva após a aplicação do herbicida glyphosate isolado e em mistura com adjuvantes na dessecação de plantas daninhas, foram instalados dois experimentos na Fazenda Experimental de Ensino e Pesquisa da Faculdade de Ciências Agrárias e Veterinárias, UNESP - campus de Jaboticabal-SP, em duas épocas: inverno de 2000 (junho - agosto) e verão de 2001 (janeiro-março). Os experimentos foram instalados no delineamento experimental de blocos ao acaso, em arranjo fatorial 4 (tratamentos herbicidas) x 5 (períodos livres de chuva simulada) + 1, com quatro repetições. Os tratamentos consistiram da combinação de glyphosate SAqC (360 g e.a. ha-1) isolado ou adicionado de uréia (50 g L-1 de calda) ou óleo vegetal (100 ml L-1 de calda) ou sulfato de amônio (100 g L-1 de calda), com cinco períodos de chuva simulada (1, 2, 4, 6 e > 48 horas após a aplicação), além de uma testemunha. A chuva foi simulada com um sistema de irrigação por aspersão, e a quantidade aplicada variou entre 18 e 19 mm. em ambas as épocas a chuva foi prejudicial à ação do glyphosate, principalmente nos menores períodos livres de chuva após a aplicação. Os sintomas de fitointoxicação apareceram mais rapidamente no verão. A utilização de adjuvantes na calda de pulverização não beneficiou o desempenho do herbicida glyphosate no controle das plantas daninhas, no inverno. A adição de uréia (50 g L¹) é uma boa alternativa para o controle de plantas daninhas, no verão, em situações sujeitas à chuva até duas horas após a aplicação.
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Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)
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Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)
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A diversidade morfológica da superfície foliar existente entre as espécies de plantas e a presença de estruturas foliares, como tricomas, estômatos, cutícula e ceras, podem exercer grande influência na aderência e deposição das gotas de pulverização, assim como na absorção do herbicida. Dessa forma, o objetivo do presente trabalho foi estudar, em plantas daninhas aquáticas emersas (Brachiaria mutica, Brachiaria subquadripara e Panicum repens), o pH foliar, bem como a área de molhamento de gotas de pulverização na superfície foliar adaxial e abaxial. O experimento foi conduzido no Núcleo de Pesquisas Avançadas em Matologia - NUPAM, pertencente à Faculdade de Ciências Agronômicas de Botucatu/SP - UNESP. As plantas foram cultivadas em caixas d'água no campo, quando elas atingiram seu pleno desenvolvimento (antes do florescimento), foram feitas as avaliações de pH foliar e da área de molhamento de gotas de pulverização. As tensões superficiais das gotas depositadas (0,5 µL), apresentadas pelas soluções de glyphosate aplicado isoladamente (5,0% v v-1, Rodeo 480g L-1 e.a. - produto comercial), glyphosate + Aterbane BR (5,0% + 0,5% v v-1), glyphosate + Silwet L-77 (5,0% + 0,05% v v-1), além das soluções com os adjuvantes isolados, Aterbane BR (0,5% v v-1) e Silwet L-77 (0,05% v v-1), foram respectivamente de 72,1; 28,7; 23,3; 37,3; e 22,1 mN m-1. As médias obtidas de pH foliar variaram entre 5,71 e 6,03, destacando-se a espécie B. mutica, com valores de 5,72 e 6,03 para as faces adaxial e abaxial, respectivamente. Contudo, mais estudos devem ser realizados para verificar a influência do pH foliar na absorção de herbicidas por espécies daninhas aquáticas. Das plantas daninhas aquáticas avaliadas, B. subquadripara foi a espécie que obteve as maiores médias de área de molhamento nas faces adaxial e abaxial da folha, proporcionadas pelas soluções de glyphosate + Aterbane BR, glyphosate + Silwet L-77 e Silwet L-77, com valores de 6,44 - 4,36; 7,77 - 10,59; e 10,94 - 10,28 mm², respectivamente.
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O objetivo deste trabalho foi avaliar os efeitos de surfatantes e pontas de pulverização na deposição da calda de pulverização em plantas de Cynodon dactylon. Os tratamentos foram dispostos em um esquema fatorial 2 x 5, sendo duas pontas de pulverização (XR 11002 e TX-VK 8) e cinco caldas de pulverização (sem surfatante e com os surfatantes Aterbane e Silwet a 0,05% e 0,1%). As caldas foram preparadas utilizando-se o corante FDC-1 a 1.500 ppm como traçador. O delineamento experimental foi o inteiramente casualizado, com 10 repetições. As aplicações foram realizadas através de um pulverizador estacionário a pressão constante e com consumo de calda de 150 L ha-1. A ponta de pulverização do tipo jato cônico vazio proporcionou maior deposição nas folhas de grama-seda, quando comparada com a ponta do tipo jato plano, independentemente do adjuvante utilizado. As maiores deposições ocorreram nas doses de 0,1%, para ambos os surfatantes, quando utilizada a ponta de jato plano e para o Silwet a 0,05% pulverizado com a ponta de jato cônico. A deposição de calda nas folhas foi menor quando da não-adição de surfatante, independentemente da ponta de pulverização utilizada.
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Petroleum is a complex combination of various classes of hydrocarbons, with paraffinic, naphtenic and aromatic compounds being those more commonly found in its composition. The recent changes in the world scenario, the large reserves of heavy oils and also the lack of new discoveries of large petroleum fields are indications that, in the near future, the oil recovery by conventional methods will be limited. In order to increase the efficiency of the extraction process, enhanced recovery methods are cited in applications where conventional techniques have proven to be little effective. The injection of surfactant solutions as an enhanced recovery method is advantageous in that surfactants are able to reduce the interfacial tensions between water and oil, thus augmenting the displacement efficiency and, as a consequence, increasing the recovery factor. This work aims to investigate the effects of some parameters that influence the surfactant behavior in solution, namely the type of surfactant, the critical micelle concentration (CMC) and the surface and interface tensions between fluids. Seawater solutions containing the surfactants PAN, PHN and PJN have been prepared for presenting lower interfacial tensions with petroleum and higher stability under increasing temperature and salinity. They were examined in an experimental apparatus designed to assess the recovery factor. Botucatu (Brazil) sandstone plug samples were submitted to assay steps comprising saturation with seawater and petroleum, conventional recovery with seawater and enhanced recovery with surfactant solutions. The plugs had porosity between 29.6 and 32.0%, with average effective permeability to water of 83 mD. The PJN surfactant, at a concentration 1000% above CMC in water, had a higher recovery factor, causing the original oil in place to be recovered by an extra 20.97%, after conventional recovery with seawater
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In the petroleum industry, water is always present in the reservoir formation together with petroleum and natural gas and this fact provokes the production of water with petroleum, resulting in a great environmental impact. Several methods can be applied for treatment of oily waters, such as: gravitational vases, granulated media filtration systems, flotation process, centrifugation process and the use of hydrocyclones, which can also be used in a combined way. However, the flotation process has showed a great efficiency as compared with other methods, because these methods do not remove great part of the emulsified oil. In this work was investigated the use of surfactants derived from vegetable oils, OSS and OGS, as collectors, using the flotation process in a glass column with a porous plate filter in its base for the input of the gaseous steam. For this purpose, oil/water emulsions were prepared using mechanical stirring, with concentrations around 300 ppm. The air flow rate was set at 700 cm3/min and the porous plate filter used for the generation of the air bubbles has pore size varying from 16 to 40 Pm. The column operated at constant volume (1500mL). A new methodology has been developed to collect the samples, where, instead of collecting the water phase, it was collected the oil phase removed by the process in the top of the flotation column. It has been observed that it is necessary to find an optimum surfactant concentration to achieve enhanced removal efficiency. Being for OSS 1.275 mmol/L and for OGS 0.840 mmol/L, with removal efficiencies of 93% and 99%, respectively, using synthetic solutions. For the produced water, the removal in these concentrations was 75% for OSS and 65% for OGS. It is possible to remove oil from water in a flotation process using surfactants of high HLB, fact that is against the own definition of HLB (Hydrophile-Lipophile Balance). The interfacial tension is an important factor in the oil removal process using a flotation process, because it has direct interference in the coalescence of the oil drops. The spreading of the oil of the air bubble should be considered in the process, and for the optimum surfactant concentrations it reached a maximum value. The removal kinetics for the flotation process using surfactants in the optimum concentration has been adjusted according to a first order model, for synthetic water as for the produced water.
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O trabalho objetivou avaliar o efeito de surfatantes em soluções aquosas sobre a tensão superficial dinâmica e ângulo de contato das gotas em diferentes superfícies: artificiais (lâmina de vidro e de óxido de alumínio) e naturais (superfícies adaxiais de folhas de Euphorbia heterophylla, Ipomoea grandifolia e Brachiaria plantaginea). Seis formulações de surfatantes (Antideriva®; Uno®; Pronto 3®; Li-700®; Supersil® e Silwet L-77®), respectivamente nas doses recomendadas do produto comercial (0,050; 0,025; 0,100; 0,250; 0,100 e 0,100 % v v-1) e o dobro delas, foram avaliadas em soluções aquosas. A tensão superficial dinâmica e o ângulo de contato formado sobre as superfícies naturais foram medidos por tensiômetro. Os ângulos de contato formados pelas gotas nas superfícies artificiais foram obtidos por análise de imagens capturadas por uma câmera digital. Os surfatantes influenciam nas propriedades físico-químicas de soluções aquosas. As soluções contendo os surfatantes Silwet L-77® e Supersil®; nas doses de 0,100 e 0,200% v v-1; proporcionaram maiores reduções na tensão superficial dinâmica e menores ângulos de contato das gotas sobre as superfícies artificiais e naturais. Os surfatantes organossiliconados em solução aquosa foram mais eficientes na redução da tensão superficial e proporcionaram maior molhamento de superfícies natural e artificial. em alvos naturais, essas propriedades obtidas com organossiliconados são dependentes das características de superfície das espécies vegetais.
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Com o objetivo de avaliar a eficiência da agregação de surfatantes ao herbicida glyphosate analisou-se a tensão superficial de diferentes soluções de pulverização contendo o hebicida e o surfatante, e a área de molhamento destas soluções nas folhas de Cyperus rotundus L.. Foram desenvolvidos métodos para avaliação da tensão superficial e da área de molhamento. Para analisar a tensão fez-se pesagens das gotas formadas na extremidade de uma bureta, com os seguintes tratamentos combinados de forma fatorial (3 x 5 x 11): 3 surfatantes (Extravon, Aterbane e Silwet L-77), 5 concentrações do herbicida, produto comercial Roundup (0; 1; 2; 3,5 e 5 %) e 11 concentrações de cada surfatantes (0; 0,005; 0,01; 0,02; 0,05; 0,1; 0,2; 0,5; 1; 2 e 3,5 %), num total de 165 tratamentos. Para avaliar a área de molhamento nas folhas de tiririca aplicou-se gotas de 0,48 .l. Os dados foram ajustados pelo modelo de Mitscherlich e, observou-se que para o surfatante Extravon que a eficiência decrescia gradativamente a medida em que aumentava a concentração do herbicida; para o Aterbane a eficiência foi reduzida apenas em baixas concentrações; já o surfatante Silwet L-77 apresentou eficiência bem superior aos demais e sua eficiência foi pouco alterada com a adição herbicida. Houve uma correlação positiva entre área de molhamento e tensão superficial. Concluiu-se, ainda, que não basta um surfatante reduzir a tensão superficial da água destilada, para que possa ser recomendado seu uso agrícola, assim, o surfatante deve ser submetido a testes preliminares com os defensivos em que serão conjugados para posterior recomendação.
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The development of new fuels is an important field of scientific and technological activities, since much of the energy consumed in the world is obtained from oil, coal and natural gas, and these sources are limited and not renewable. Recently it has assessed the employment of microemulsions as an alternative for obtaining fuel isotropic between phases originally not miscible. Among many advantages, emphasizes the application of substances that provide the reduction of levels of emissions compared to fossil fuels. Thus, this work was a study of various microemulsified systems, aiming to check the performance of the winsor regions front of the use of surfactants: RENEX 18 → 150, UNITOL L-60 → L-100 and AMIDA 60, together with structure of esters from soybean and castor bean oils. From the results it were chosen four systems to physico-chemical analyzes: System I RENEX 60, Soil bean oil, methylic ester (EMOS) and water; System II RENEX 60/AMIDA 60, EMOS and water; System III RENEX 70, mamona oil methylic ester (EMOM) and water and System IV RENEX 95, EMOM and water. The tests of physico-chemical characterization and study of temperature increase were done with nine points with different compositions in a way to include the interest area (microemulsion W/O). After this study, was conducted a modeling to predict the viscosity, the property is more varied as function of compositions systems changes. The best results were the systems II and IV with a temperature stability above 60°C. The system I had its physico-chemical characterization very similar to a fossil fuel. The system II was the best one due to its corrosivity be stable. In the modeling the four systems had shown good, with an error that varied between 5 and 18%, showing to be possible the viscosity prediction from the composition of the system. The effects the microemulsion and the engine´s performance with the microemulsion were also avaliated. The tests were performed in a cycle-diesel engine. The potency and consumption were analysed. Results show a slight increase the rendiment fuel compared with the conventional as well as a decrease in specific consumption
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The formation of paraffin deposits is common in the petroleum industry during production, transport and treatment stages. It happens due to modifications in the thermodynamic variables that alter the solubility of alkanes fractions present in petroleum. The deposition of paraffin can provoke significant and growing petroleum losses, arriving to block the flow, hindering to the production. This process is associated with the phases equilibrium L-S and the stages and nucleation, growth and agglomeration the crystals. That process is function of petroleum intrinsic characteristics and temperature and pressure variations, during production. Several preventive and corrective methods are used to control the paraffin crystallization, such as: use of chemical inhibitors, hot solvents injection, use of termochemistry reactions, and mechanical removal. But for offshore exploration this expensive problem needs more investigation. Many studies have been carried through Wax Appearance Temperature (WAT) of paraffin; therefore the formed crystals are responsible for the modification of the reologics properties of the oil, causing a lot off operational problems. From the determination of the WAT of a system it is possible to affirm if oil presents or not trend to the formation of organic deposits, making possible to foresee and to prevent problems of wax crystallization. The solvent n-paraffin has been widely used as fluid of perforation, raising the production costs when it is used in the removal paraffin deposits, needing an operational substitute. This study aims to determine the WAT of paraffin and the interference off additives in its reduction, being developed system paraffin/solvent/surfactant that propitiates the wax solubilization. Crystallization temperatures in varied paraffin concentrations and different solvents were established in the first stage of the experiments. In the second stage, using the methodology of variation of the photoelectric signal had been determined the temperature of crystallization of the systems and evaluated the interferences of additives to reduction of the WAT. The experimental results are expressed in function of the variations of the photoelectric signals during controlled cooling, innovating and validating this new methodology to determine WAT, relatively simple with relation the other applied that involve specific equipments and of high cost. Through the curves you differentiate of the results had been also identified to the critical stages of growth and agglomeration of the crystals that represent to the saturation of the system, indicating difficulties of flow due to the increase of the density
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Petroleum can be associated or not with natural gas, but in both cases water is always present in its formation. The presence of water causes several problems, such as the difficulty of removing the petroleum from the reservoir rock and the formation of waterin-oil and oil-in-water emulsions. The produced water causes environmental problems, which should be solved to reduce the effect of petroleum industry in the environment. The main objective of this work is to remove simultaneously from the produced water the dispersed petroleum and dissolved metals. The process is made possible through the use of anionic surfactants that with its hydrophilic heads interacts with ionized metals and with its lipophilic tails interacts with the oil. The studied metals were: calcium, magnesium, barium, and cadmium. The surfactants used in this research were derived from: soy oil, sunflower oil, coconut oil, and a soap obtained from a mixture of 5wt.% coconut oil and 95wt.% animal fat. It was used a sample of produced water from Terminal de São Sebastião, São Paulo. As the concentration of the studied metals in produced water presented values close to 300 mg/L, it was decided to use this concentration as reference for the development of this research. Molecular absorption and atomic absorption spectroscopy were used to determine petroleum and metals concentrations in the water sample, respectively. A constant pressure filtration system was used to promote the separation of solid and liquid phases. To represent the behavior of the studied systems it was developed an equilibrium model and a mathematical one. The obtained results showed that all used surfactants presented similar behavior with relation to metals extraction, being selected the surfactant derived from soy oil for this purpose. The values of the partition coefficients between the solid and liquid phases " D " for the studied metals varied from 0.2 to 1.1, while the coefficients for equilibrium model " K " varied from 0.0002 and 0.0009. The removal percentile for oil with all metals associated was near 100%, showing the efficiency of the process