Deposição e distribuição de calda de pulverização em plantas de feijoeiro (Phaseolus vulgaris) e capim-braquiária (Brachiaria decumbens)

Com o objetivo de avaliar a deposição e distribuição de solução traçante em plantas de feijoeiro e capim-braquiária, foi conduzido experimento no NuPAM-FCA/ UNESP, campus de Botucatu-SP, utilizando um simulador de pulverização em ambiente controlado. Os tratamentos utilizados foram: bico jato plano XR Teejet (XR110.02VS) + surfactante Aterbane BR (0,5% v/v); bico jato cônico Conejet (TXVK-4) + surfactante Aterbane BR (0,5% v/v); bico jato plano XR Teejet (XR110.02VS); e bico jato cônico Conejet (TXVK-4). em todos os tratamentos foi aplicada uma solução de NaCl (0,5% p/v) + corante Poliglow laranja (0,5% p/v) + mancozeb (0,5% p/v). As unidades experimentais constituíram-se de vasos com duas plantas-alvo de capim-braquiária posicionadas sob uma planta-alvo de feijoeiro. A visualização da distribuição das gotas nas folhas de capim-braquiária foi efetuada com auxílio de luz negra, e o depósito da calda na superfície das plantas foi quantificado através da condutividade elétrica da solução aplicada e coletada por meio de lavagem de ambos os alvos. Os bicos de pulverização, jato plano (XR Teejet) e cônico (Conejet), não apresentaram diferença no depósito nos folíolos totais de feijoeiro quando submetidos a mesma condição de calda de pulverização. No entanto, o bico jato plano XR Teejet (XR110.02VS) e o bico jato cônico Conejet (TXVK-4) proporcionaram aumento de 67,1 e 61,5% na deposição da calda em relação a área foliar e 106,4 e 66,9% para matéria seca, respectivamente, em relação ao bico jato plano XR Teejet (XR110.02VS) + surfactante Aterbane BR (0,5% v/v) e ao bico jato cônico Conejet (TXVK-4) + surfactante Aterbane BR (0,5% v/v). Para o capim-braquiária, o bico cônico Conejet proporcionou deposição superior e distribuição mais uniforme em relação ao jato plano XR Teejet.

Depósitos unitários de calda de pulverização com e sem surfatante em plantas de Salvinia molesta

Uma das opções para o manejo de Salvina molesta é o controle químico; contudo, a presença de grande quantidade de pêlos na epiderme foliar reduz a molhabilidade das folhas, o que pode afetar a eficiência dos herbicidas. O objetivo deste trabalho foi o de avaliar a deposição do corante azul FDC-1, no qual se simulou a aplicação de herbicidas em plantas dessa espécie, com e sem a mistura de um surfatante. Os tratamentos foram as concentrações de 0 e 5% do surfatante Aterbane (espalhante adesionante), utilizado na elaboração da calda de pulverização. O delineamento experimental foi o inteiramente casualizado, com 150 repetições. A aplicação foi realizada com um pulverizador estacionário à pressão de 2,0 bar, com consumo de calda de 180 L ha-1. Foram utilizados bicos de jato plano, tipo XR 110.02. Foram ajustadas curvas de regressão entre os depósitos individuais em cada planta (mL calda/planta) e as freqüências acumuladas. Utilizou-se o modelo de Gompertz, e os valores de R² foram de 0,99 e 0,97 com e sem o espalhante, respectivamente. em termos médios, a adição de Aterbane reduziu em 1,13% os depósitos do FDC-1. No entanto, o espalhante melhorou em 76, 41 e 29% a deposição em 1, 5 e 10% da população com menores depósitos do corante.

Depósitos de calda de pulverização nas faces adaxial e abaxial de folhas de Eichhornia crassipes dispostas em diferentes ângulos

Estudos foram conduzidos com o objetivo de avaliar os depósitos de gotas pulverizadas através de dois tipos de pontas sobre as faces adaxial e abaxial de folhas de Eichhornia crassipes dispostas em diferentes ângulos. No primeiro estudo, os tratamentos foram dispostos no esquema fatorial 2x4x7: dois tipos de pontas (TX12 e XR11002VS), quatro ângulos verticais (0º, 30º, 60º e 90º) e sete ângulos horizontais (0º, 15º, 30º, 45º, 60º, 75º e 90º). No ângulo vertical de 90º a lâmina foliar foi posicionada paralelamente ao sentido de deslocamento do jato de pulverização; e no ângulo horizontal de 90º a folha foi posicionada perpendicularmente ao plano do solo. Como traçadores, foram utilizadas soluções de 1.000 ppm do corante Azul FDC-1 e 3.500 ppm do corante Amarelo Tartrasina para as pontas tipo leque e cone, respectivamente. No segundo estudo, os tratamentos foram dispostos no esquema fatorial 2x2x3: dois tipos de pontas (TX12 e XR11002VS), dois tipos de calda (com e sem Aterbane BR a 0,5%) e três ângulos horizontais (0º, 45º e 90º). Adotou-se o ângulo vertical de 90º como padrão para todos os tratamentos. Soluções de 1.000 ppm do corante Azul FDC-1 e 3.500 ppm do corante Amarelo Tartrasina foram utilizadas como traçadores para a calda com e sem surfatante, respectivamente. Os resultados do primeiro estudo revelaram que os depósitos observados em toda a folha e na face adaxial das lâminas foliares de aguapé diminuíram à medida que se aumentou a angulação vertical, independentemente da ponta utilizada. Os menores depósitos sempre estiveram relacionados ao ângulo vertical de 90º, independentemente do ângulo horizontal utilizado. Não foi detectado nenhum depósito na face abaxial das folhas de aguapé em todas as combinações dos fatores estudados. No segundo estudo também foram observados os mesmos decréscimos no volume de calda depositado em toda a folha e na face adaxial à medida que se aumentou a angulação vertical das lâminas foliares. As duas pontas proporcionaram depósitos nulos na face abaxial quando o surfatante não foi utilizado; entretanto, a adição do surfatante à calda incrementou significativamente os depósitos nesta face da folha do aguapé.

Controle químico de plantas daninhas aquáticas: Alternanthera philoxeroides, Enhydra anagallis e Pycreus decumbens

As espécies de plantas aquáticas podem causar inúmeros inconvenientes ao uso múltiplo da água quando elas se desenvolvem desordenadamente. Assim, o objetivo deste trabalho foi avaliar a eficiência de diferentes herbicidas no controle químico de plantas de Alternanthera philoxeroides, Enhydra anagallis e Pycreus decumbens em caixa-d'água. Quando as plantas atingiram o seu pleno desenvolvimento (antes do florescimento), foram aplicados, nas espécies Alternanthera philoxeroides e Enhydra anagallis, os herbicidas: 2,4-D amina (U-46 D FLUID 720) a 2.880 g e.a. ha-1; diquat (REWARD 240) a 480 g i.a. ha-1; imazapyr (ARSENAL 250) a 500 e 750 g e.a. ha-1; glyphosate (RODEO 480) a 3.360 g e.a. ha-1 com e sem o surfatante Aterbane BR (0,5% v v-1); glyphosate + diquat (3.360 + 480 g i./e.a. ha-1 ); glyphosate + 2,4-D (3.360 + 2.880 g e.a. ha-1); e diquat + 2,4-D (480 + 2.880 g i./e.a. ha-1), além de uma testemunha sem aplicação de herbicida. Para a espécie Pycreus decumbens foram aplicados: 2,4-D amina (U-46 D FLUID 720) a 2.880 g e.a. ha-1; diquat (REWARD 240) a 480 g i.a. ha-1; propanil (STAM 480) a 2.880 g i.a. ha-1; glyphosate (RODEO 480) a 3.360 g e.a. ha-1 mais o surfatante Aterbane BR (0,5% v v-1); glyphosate + propanil (3.360 + 2.880 g i./e.a. ha-1); glyphosate + diquat (3.360 + 480 g i./e.a. ha-1); glyphosate + 2,4-D (3.360 + 2.880 g e.a. ha-1); propanil + 2,4-D (2.880 + 2.880 g i./e.a. ha-1); e diquat + 2,4-D (480 + 2.880 g i./e.a. ha-1), além de uma testemunha sem aplicação de herbicida. Os herbicidas foram aplicados com um pulverizador estacionário, pressurizado a ar comprimido e equipado com um reservatório de 2 litros, pontas Teejet XR11002VS, com um consumo de calda de 200 L ha-1. As avaliações de controle das plantas daninhas foram visuais, por meio de uma escala de percentual de notas, além de se avaliar a massa seca das plantas. Verificou-se que o controle químico apresenta-se como uma boa alternativa de manejo para as espécies A. philoxeroides, E. anagallis e P. decumbens, e a mistura de herbicidas pode aumentar a eficiência de controle. E. anagallis apresentou alta sensibilidade à ação dos herbicidas; entretanto, as espécies A. philoxeroides e P. decumbens evidenciaram alta capacidade de regeneração, principalmente quando se utilizaram herbicidas de ação de contato.

Efeito de diferentes concentrações de aterbane na deposição de calda em plantas de Pistia stratiotes

O objetivo deste trabalho foi avaliar o efeito do adjuvante Aterbane na deposição de calda de pulverização, aplicada sobre plantas de Pistia stratiotes. Os tratamentos foram constituídos por três concentrações do adjuvante Aterbane (0, 0,25 e 0,5%), usado na elaboração da calda de pulverização. As caldas foram preparadas utilizando-se o corante FDC-1 a 1.500 ppm como traçante. O delineamento experimental adotado foi o inteiramente casualizado com 30 repetições, sendo cada repetição constituída por uma planta com seis folhas. A aplicação foi feita com um pulverizador estacionário, à pressão constante de 2 bars, com consumo de calda de 200 L ha-1. Foram utilizadas pontas de jato plano Teejet 11002vs. Os resultados demonstraram que, quantitativamente, o Aterbane não promoveu nenhum efeito na deposição da calda, entretanto, qualitativamente, quanto maior a concentração utilizada maior foi a uniformidade de deposição de calda.

Influência dos Íons Mg, Ca, Fe, Cu e Zn sobre a tensão superficial estática de soluções contendo surfatante

O objetivo do estudo foi avaliar a influência da presença de cinco íons em uma calda de pulverização contendo o surfatante Aterbane. A tensão superficial foi analisada por meio da medição da massa de um conjunto de 25 gotas, com quatro repetições constituindo um tratamento. O trabalho foi dividido em duas etapas. Na primeira, os tratamentos foram combinados em esquema fatorial 9x5x2, sendo nove concentrações do surfatante Aterbane (0,01; 0,025; 0,05; 0,1; 0,2; 0,5; 1; 2; e 3%), cinco íons (Mg++, Ca++, Fe+++, Cu+++ e Zn+++) e duas concentrações desses elementos (10 e 100 ppm). Na segunda etapa, os tratamentos foram combinados em esquema fatorial 5x5x1, utilizandose os mesmos cinco elementos (Mg++, Ca++, Fe+++, Cu+++ e Zn+++), em cinco concentrações (1, 5, 20, 50 e 200 ppm), com apenas uma concentração do surfatante Aterbane (0,025%). Outros nove tratamentos permitiram avaliar as tensões superficiais das concentrações do surfatante (0,01; 0,025; 0,05; 0,1; 0,2; 0,5; 1; 2; e 3%) sem a adição dos íons. Os resultados mostraram que houve interferência dos íons sobre as soluções, já que, com exceção do Fe+++ (na concentração de 10 e 100 ppm) e do Cu+++ (na concentração de 100 ppm), todos os íons reduziram a tensão mínima alcançada e aumentaram a eficiência do surfatante, implicando benefícios à ação do surfatante e sobre as características de possíveis soluções de aplicação. Todos os íons avaliados promoveram reduções nas tensões superficiais de soluções do surfatante na concentração de 0,025%.

Estudo das propriedades físico-químicas de biocombustíveis microemulsionados

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

Avaliação da temperatura de cristalização da parafina em sistemas: parafina, solvente e tensoativo

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

Purificação da glicerina bruta obtida a partir da transesterificação do óleo de algodão

The crude glycerine is a raw material that can be used in a wide variety of products. Even with all the impurities inherent in the process of being obtained, the crude glycerin is already in a marketable product. However, the market is much more favorable to the commercialization of purified glycerine. The glycerin is a byproduct gotten from the process of transesterification of waste oils and fats in the production of biodiesel. More recently, the deployment of the new Federal Law of Brazil, related to the implementation of energy resources, forces, from 2008, the increase of 2% biodiesel in diesel common with prospects for 5% (B5). Therefore, it is indispensable that new routes of purification as well as new markets are developed. The objective of this work was to purify, through ion exchange, the crude glycerin, obtained from the reaction of transesterification of cottonseed oil. The cottonseed oil was characterized as the fatty acid composition and physical-chemical properties. The process of ion exchange was conducted in batch. In this process were used strong cation, low anion resins and a mixed resin used to de-ionize water. The purified glycerin was characterized as the content of metals. Tests were performed with activated charcoal adsorption, and for this, it was made tests of time contact with coal as well as quantity of coal used. The time of activation, the amount of the activation solution, the contact time of the glycerol solution in resins, the amount and type of resin applied were evaluated. Considering the analysis made with activated charcoal, when the glycerin solution was treated using the resins individually it was observed that in the conditions for treatment with 10 g of resin, 5 hours of contact with each resin and 50 mL of glycerin solution, its conductivity decreased to a cationic resin, increased to the anionic resin and had a variable value with respect to resin mixed. In the treatment in series, there was a constant decrease in the conductivity of the solution of glycerin. Considering two types of treatment, in series and individually, the content of glycerol in glycerin pre-purified solution with the different resins varied from 12,46 to 29.51% (diluted solution). In analysis performed without the use of activated charcoal, the behavior of the conductivity of the solution of glycerin were similar to results for treatment with activated charcoal, both in series as individually. The solution of glycerin pre-purified had a glycerol content varying from 8.3 to 25.7% (diluted solution). In relation to pH, it had a behavior in accordance with the expected: acid for the glycerin solution treated with cationic resin, basic when the glycerin solution was treated with the anionic resin and neutral when treated with the mixed resin, independent of the kind of procedure used (with or without coal, resins individually or in series). In relation to the color of the glycerin pre-purified solution, the resin that showed the best result was the anionic (colorless), however this does not mean that the solution is more in pure glycerol. The chromatographic analysis of the solutions obtained after the passage through the resins indicated that the treatment was effective by the presence of only one component (glycerol), not considering the solvent of the analysis

Avaliação da molhabilidade de soluções de tensoativos em aço inoxidável

With the increasing industrialization of the planet caused by globalization, it has become increasingly common to search for highly resistant and durable materials for many diverse branches of activities. Thus, production and demand for materials that meet these requirements have constantly increased with time. In view of this, stainless steel is presented as one of the materials which are suitable applications, due to many features that are interesting for several segments of the industry. Concerns of oil companies over heavy oil reservoirs have grown steadily for the last decades. Rheological properties of these oils impair their transport in conventional flow systems. This problem has created the need to develop technologies to improve flow and transport, reducing operation costs so as to enable oil production in the reservoir. Therefore, surfactant-based chemical systems are proposed to optimize transport conditions, effected by reduction of interfacial tensions, thereby enhancing the flow of oil in ducts and reducing load losses by friction. In order to examine such interactions, a study on the wettability of metallic surfaces has been undertaken, represented by measuring of contact angle of surfactant solutions onto flat plates of 304 stainless steel. Aqueous solutions of KCl, surfactants and mixtures of surfactants, with linear and aromatic hydrocarbon chain and ethoxylation degrees ranging between 20 to 100, have been tested. The wettability was assessed by means of a DSA 100 krüss goniometer. The influence of roughness on the wettability was also investigated by machining and polished the stainless steel plates with sandpapers of references ranging between 100 of 1200. The results showed that sanding and polishing plates result in decrease of wettability. As for the solutions, they have provided better wettability of the stainless steel than the KCl solutions tested. It was also been concluded that surfactant mixtures is an option to be considered, since they promote interactions that generate satisfactory contact angles for a good wettability on the stainless steel plate. Another conclusion refers to the influence of the ethoxylation degree of the nonionic surfactant molecules on wettability. It has been observed that contact angles decrease with decreasing ethoxylation degrees. This leads us to conclude that molecules with higher ethoxylation degree, being more hydrophobic, decrease the interaction of water with the ducts, thereby reducing friction and improving the flow

Análise dos Processos de Flotação e Oxidação Avançada para o Tratamento de Efluente Modelo da Indústria do Petróleo

The generation of wastes in most industrial process is inevitable. In the petroleum industry, one of the greatest problems for the environment is the huge amount of produced water generated in the oil fields. This wastewater is a complex mixture and present great amounts. These effluents can be hazardous to the environmental without adequate treatment. This research is focused in the analysis of the efficiencies of the flotation and photo-oxidation processes to remove and decompose the organic compounds present in the produced water. A series of surfactants derivated from the laurilic alcohol was utilized in the flotation to promote the separation. The experiments have been performed with a synthetic wastewater, carefully prepared with xylene. The experimental data obtained using flotation presented a first order kinetic, identified by the quality of the linear data fitting. The best conditions were found at 0.029 g.L-1 for the surfactant EO 7, 0.05 g.L-1 for EO 8, 0.07 g.L-1 for EO 9, 0.045 g.L-1 for EO 10 and 0.08 g.L-1 for EO 23 with the following estimated kinetic constants: 0.1765, 0.1325, 0.1210, 0.1531 and 0.1699 min-1, respectively. For the series studied, the most suitable surfactant was the EO 7 due to the lower reagent onsumption, higher separation rate constant and higher removal efficiency of xylene in the aqueous phase (98%). Similarly to the flotation, the photo-Fenton process shows to be efficient for degradation of xylene and promoting the mineralization of the organic charge around 90% and 100% in 90 min

Reciclagem de material asfáltico fresado utilizando solventes e microemulsões

With the increase of asphalt milling services was also a significant increase in recycling services pavements. The techniques used today are basically physical processes in which the milled material is incorporated into new asphalt mixtures or executed on site, with the addition of virgin asphalt and rejuvenating agent. In this paper seeks to analyze the efficiency of extraction of CAP (Petroleum Asphalt Cement) mixtures from asphalt milling, using commercial solvents and microemulsions. The solvents were evaluated for their ability to solubilize asphalt using an extractor reflux-type apparatus. Pseudoternary diagrams were developed for the preparation of microemulsion O/W surfactant using a low-cost coconut oil saponified (OCS). Microemulsions were used to extract the CAP of asphalt through physicochemical process cold. Analysis was performed concentration of CAP in solution by spectroscopy. The data provided in the analysis of concentration by the absorbance of the solution as the basis for calculating the percentage of extraction and the mass flow of the CAP in the solution. The results showed that microemulsions prepared with low concentration of kerosene and butanol/OCS binary has high extraction power of CAP and its efficiency was higher than pure kerosene, reaching 95% rate of extraction

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.

Extração de ferro da cera de carnaúba utilizando sistemas microemulsionados

The constant search for biodegradable materials for applications in several fields shows that carnauba wax can be a viable alternative in the manufacturing of biolubricants. Carnauba wax is the unique among the natural waxes to have a combination of properties of great importance. In previous studies it was verified the presence of metals in wax composition that can harm the oxidative stability of lubricants. Considering these factors, it was decided to develop a research to evaluate iron removal from carnauba wax, using microemulsion systems (Me) and perform the optimization of parameters, such as: extraction pH, temperature, extraction time, among others. Iron concentration was determined by atomic absorption and, to perform this analysis, sample digestion in microwave oven was used, showing that this process was very efficient. It was performed some analysis in order to characterize the wax sample, such as: attenuated total reflectance infrared spectroscopy (ATR-IR), thermogravimetry (TG), differential scanning calorimetry (DSC), energy dispersive X-ray fluorescence (EDXRF), scanning electron microscopy (SEM) and melting point (FP). The microemulsion systems were composed by: coconut oil as surfactant, n-butanol as cosurfactant, kerosene and/or heptanes as oil phase, distilled water as water phase. The pH chosen for this study was 4.5 and the metal extraction was performed in finite experiments. To evaluate Me extraction it was performed a factorial design for systems with heptane and kerosene as oil phase, also investigating the influence of temperature time and wax/Me ratio, that showed an statistically significant answer for iron extraction at 95% confidence level. The best result was obtained at 60°C, 10 hours contact time and 1: 10 wax/Me ratio, in both systems with kerosene and heptanes as oil phase. The best extraction occurred with kerosene as oil phase, with 54% iron removal

Modelagem da transferência de massa na remoção do óleo da água produzida por flotação em coluna com uso de tensoativos de origem vegetal

The treatment of oil produced water and its implications are continually under investigation and several questions are related to this subject. In the Northeast Region Brazil, the onshore reservoirs are, in its majority, mature oil fields with high production of water. As this oil produced water has high levels of oil, it cannot be directly discarded into the environment because it represents a risk for contamination of soil, water, and groundwater, or even may cause harm to living bodies. Currently, polyelectrolytes that promote the coalescence of the oil droplets are used to remove the dispersed oil phase, enhancing the effectiveness of the flotation process. The non-biodegradability and high cost of polyelectrolytes are limiting factors for its application. On this context, it is necessary to develop studies for the search of more environmentally friendly products to apply in the flotation process. In this work it is proposed the modeling of the flotation process, in a glass column, using surfactants derived from vegetal oils to replace the polyelectrolytes, as well as to obtain a model that represents the experimental data. In addition, it was made a comparative study between the models described in the literature and the one developed in this research. The obtained results showed that the developed model presented high correlation coefficients when fitting the experimental data (R2 > 0.98), thus proving its efficiency in modeling the experimental data.