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

Controle feedback de nível baseado em sensor de imagem aplicado ao equipamento misturador-decantador à inversão de fases (MDIF®)

The treatment of wastewaters contaminated with oil is of great practical interest and it is fundamental in environmental issues. A relevant process, which has been studied on continuous treatment of contaminated water with oil, is the equipment denominated MDIF® (a mixer-settler based on phase inversion). An important variable during the operation of MDIF® is the water-solvent interface level in the separation section. The control of this level is essential both to avoid the dragging of the solvent during the water removal and improve the extraction efficiency of the oil by the solvent. The measurement of oil-water interface level (in line) is still a hard task. There are few sensors able to measure oil-water interface level in a reliable way. In the case of lab scale systems, there are no interface sensors with compatible dimensions. The objective of this work was to implement a level control system to the organic solvent/water interface level on the equipment MDIF®. The detection of the interface level is based on the acquisition and treatment of images obtained dynamically through a standard camera (webcam). The control strategy was developed to operate in feedback mode, where the level measure obtained by image detection is compared to the desired level and an action is taken on a control valve according to an implemented PID law. A control and data acquisition program was developed in Fortran to accomplish the following tasks: image acquisition; water-solvent interface identification; to perform decisions and send control signals; and to record data in files. Some experimental runs in open-loop were carried out using the MDIF® and random pulse disturbances were applied on the input variable (water outlet flow). The responses of interface level permitted the process identification by transfer models. From these models, the parameters for a PID controller were tuned by direct synthesis and tests in closed-loop were performed. Preliminary results for the feedback loop demonstrated that the sensor and the control strategy developed in this work were suitable for the control of organic solvent-water interface level

Projeto e Operação em Escala Semi-Industrial de um Equipamento para Tratamento de Águas Produzidas na Indústria do Petróleo Utilizando Nova Tecnologia: misturador-decantador à inversão de fases - MDIF

The aim of this work is to use a new technology in the treatment of produced wastewaters from oil industry. An unit for treat produced waters called UTMDIF, was designed, installed and operated in an industrial plant for treatment of effluents from oil industry. This unit operates by means of the method of separation of phase inversion and can become a promising alternative to solve the problem of oil/water separation. This method constitutes the basis of the working of a new design of mixersettler of vertical configuration which occupies small surface area. The last characteristic becomes specially important when there is limitation on the lay-out of the plant, for example, over maritime platforms to explore oil. This equipment in a semi-industrial scale treats produced wastewaters contaminated with oil at low concentrations (ranging from 30 to 150 mg/L) and throughputs of 320 m3/d (47,4 m3 m-2 h-1). Good results were obtained in oil/water separation which leads to the necessary specification to discharge those wastewaters. Besides, the non dependence of the efficiency of separation in spite of the salinity of the medium becomes the equipment an attractive new technology to treat wastewaters containing oil at low concentrations

Viabilidade de uso de um misturador para a análise de propriedades reológicas de produtos alimentícios

Pós-graduação em Agronomia (Energia na Agricultura) - FCA

Misturador para análise de propriedades reológicas

This study aimed to evaluate the use of a mixer to determine the rheological properties of fluids. The mixer is comprised of an agitation tank and an anchor type impeller. The tests were performed with honey and fruit juices (orange, guava and peach). The rheological characterization was performed using data from the torque and rotation speed required for the operation of fluid agitation. Tests were also made with a concentric cylinder rotational viscometer with the samples being subjected to various shear rates. The rheological parameters were obtained from the flow curves fitted to the power law model. Analyses of results showed that the mixer can be used, within its limitations, to determine rheological properties.

Avaliação da biodegradabilidade de compósitos à base de poliéster e amido com fibra de coco verde

Os materiais poliméricos tem sido uma das causas dos problemas ambientais discutidos em todo mundo nos últimos tempos. Como uma das soluções para esse problema, estão os polímeros biodegradáveis que são materiais que se degradam pela ação de microorganismos. Uma Indústria sediada no Brasil lançou recentemente um poliéster biodegradável que surge boa alternativa para o crescimento no mercado dos polímeros biodegradáveis, principalmente por possuir em sua composição matéria prima de fonte renovável. Neste trabalho foram preparados compósitos com matriz de poliéster biodegradável e fibra de coco verde com e sem modificação química por acetilação em misturador interno Haake. Foi estudada a biodegradabilidade em solo simulado do polímero puro e de seus compósitos e foram avaliadas as propriedades térmicas, morfológicas e mecânicas do polímero puro e de alguns de seus compósitos. O teste de biodegradabilidade foi feito pelo enterro das amostras em solo simulado por períodos distintos, variando de duas a dezessete semanas, seguindo a Norma ASTM G 160 03. Após cada período de teste, as amostras foram retiradas do solo e analisadas por microscopia ótica (MO), microscopia eletrônica de varredura (MEV), análise termogravimétrica (TGA), calorimetria diferencial de varredura (DSC), espectroscopia na região do infravermelho (FTIR) e análise mecânica de tração. Os resultados obtidos indicaram que tanto o polímero puro quanto os seus compósitos sofreram biodegradação, a presença da fibra apenas atrasa o processo de biodegradação, as fibras de coco tiveram uma boa afinidade com a matriz polimérica, a incorporação de 5% fibra de coco na matriz torna o compósito mais rígido e a incorporação da fibra e o processo de biodegradação alteram as características da fase cristalina no material polimérico.

Otimização de reator sequencial em batelada para remoção biológica de carbono e nitrogênio com controle difuso

Este trabalho apresenta a estruturação de um controle difuso, para a automação de reatores seqüenciais em batelada (RSB), no processo de remoção biológica de matéria orgânica e nitrogênio em águas residuárias domésticas, utilizando parâmetros inferenciais, pH, ORP e OD, em que as variáveis controladas foram as durações da reação aeróbia e anóxica. O experimento, em escala de bancada, foi composto por dois reatores seqüenciais em batelada, com volume útil de 10 L, no qual 6 L foram alimentados com esgoto sintético, com características de águas residuárias domésticas. O sistema de automação foi composto pela aquisição dos parâmetros eletroquímicos (pH, ORP e OD), pelos dispositivos atuadores (motor-bomba, aerador e misturador) e pelo controle predeterminado ou difuso. O programa computacional CONRSB foi implementado de forma a integrar o sistema de automação. O controle difuso, implementado, foi constituído pelos procedimentos de: normalização, nebulização, inferência, desnebulização e desnormalização. As variáveis de entrada para o controlador difuso, durante o período: aeróbio foram dpH/dt, dpH/d(t-1) e o pH ; anóxico foram dORP/dt, dORP/d(t-1) e o OD. As normalizações das variáveis crisps estiveram no universo de [0,1], utilizando os valores extremos do ciclo 1 ao 70. Nas nebulizações foram aplicadas as funções triangulares, as quais representaram, satisfatoriamente, as indeterminações dos parâmetros. A inferência nebulosa foi por meio da base heurística (regras), com amparo do especialista, em que a implicação de Mamdani foi aplicada Nessas implicações foram utilizadas dezoito expressões simbólicas para cada período, aeróbio e anóxico. O método de desnebulização foi pelo centro de áreas, que se mostrou eficaz em termos de tempo de processamento. Para a sintonia do controlador difuso empregou-se o programa computacional MATLAB, juntamente com as rotinas Fuzzy logic toolbox e o Simulink. O intervalo entre as atuações do controlador difuso, ficou estabelecido em 5,0 minutos, sendo obtido por meio de tentativas. A operação do RSB 1, durante os 85 ciclos, apresentou a relação média DBO/NTK de 4,67 mg DBO/mg N, sendo classificado como processo combinado de oxidação de carbono e nitrificação. A relação média alimento/microrganismo foi de 0,11 kg DBO/kg sólido suspenso volátil no licor misto.dia, enquadrando nos sistemas com aeração prolongada, em que a idade do lodo correspondeu aos 29 dias. O índice volumétrico do lodo médio foi de 117,5 mL/g, indicando uma sedimentação com características médias. As eficiências médias no processo de remoção de carbono e nitrogênio foram de 90,8% (como DQO) e 49,8%, respectivamente. As taxas específicas médias diárias, no processo de nitrificação e desnitrificação, foram de 24,2g N/kg SSVLM.dia e 15,5 g N/kg SSVLM.dia, respectivamente. O monitoramento, em tempo real, do pH, ORP e OD, mostrou ter um grande potencial no controle dos processos biológicos, em que o pH foi mais representativo no período aeróbio, sendo o ORP e o OD mais representativos no período anóxico. A operação do RSB com o controlador difuso, apresentou do ciclo 71 ao 85, as eficiências médias no processo de remoção de carbono e nitrogênio de 96,4% (como DQO) e 76,4%, respectivamente. A duração média do período aeróbio foi de 162,1 minutos, que tomando como referência o período máximo de 200,0 minutos, reduziu em 19,0% esses períodos. A duração média do período anóxico foi de 164,4 minutos, que tomando como referência o período máximo de 290,0 minutos, apresentou uma redução de 43,3%, mostrando a atuação robusta do controlador difuso. O estudo do perfil temporal, no ciclo 85, mostrou a atuação efetiva do controlador difuso, associada aos pontos de controle nos processos biológicos do RSB. Nesse ciclo, as taxas máximas específicas de nitrificação e desnitrificação observadas, foram de 32,7 g NO3 --N/kg sólido suspenso volátil no licor misto.dia e 43,2g NO3 --N/kg sólido suspenso volátil no licor misto.dia, respectivamente.

Desenvolvimento de elastômeros termoplásticos a partir de SBR epoxidada e polipropileno

Os elastômeros termoplásticos vulcanizados (TPVs) na sua maioria constituídos por borrachas apolares (EPDM, NR) e poliolefinas (PP, PE), apresentam a vantagem de serem processáveis como termoplásticos e serem facilmente reciclados. No entanto, apresentam desvantagens no que se refere à sua baixa resistência a óleos, combustíveis e graxas em relação à borracha termofixa. Este trabalho, teve como objetivo estudar a obtenção de TPVs com propriedades mecânicas adequadas e resistência a óleos e solventes orgânicos, a partir da borracha comercial SBR 1502 parcialmente epoxidada. Esta, por ter a estrutura química de sua cadeia principal modificada pela introdução de grupos epóxidos, deve apresentar melhor resistência a óleos e solventes. Os TPVs foram obtidos em misturador fechado acoplado a um reômetro Haake, na temperatura de 1800C e velocidade de rotor de 75 rpm, vulcanizados dinamicamente com o sistema Bismaleimida/peróxido de dicumila. Foram caracterizados quanto às suas propriedades mecânicas por medidas tensão-deformação, medidas mecânicas dinâmicas, inchamento em ciclohexano, THF e óleo IRM 903, dureza. A morfologia foi determinada por microscopia eletrônica de varredura, MEV. Foram analisados os fatores que influenciam as propriedades dos TPVs, tais como composição (relação PP/SBR), teor de BMI, grau de epoxidação da borracha, uso de agente compatibilizante. O TPV na composição PP/SBR 40/60, esta epoxidada em 40 mol % e contendo o agente compatibilizante Vestenamer adicionado na forma de blenda (borracha/agente compatibilizante) apresentou a melhor resposta em termos de tensão-deformação na ruptura. Os TPVs com a SBR epoxidada em 70% apresentaram melhor resistência a óleo e solventes. Os fatores, potencialmente, capazes de influenciar a dureza dos TPVs também foram avaliados. Neste particular, verificou-se que o tipo de poliolefina, bem como o uso de plastificante são os fatores que mais influenciam a dureza dos TPVs.

Vórtex

Este modelo é parte de um conjunto de modelos 3D produzidos pela equipe de audiovisual da SEaD/UFSCar para o jogo de realidade virtual “O Laboratório de Química”.

Homogeneizador de Amostras em Y

Este modelo é parte de um conjunto de modelos 3D produzidos pela equipe de audiovisual da SEaD/UFSCar para o jogo de realidade virtual “O Laboratório de Química”.

Compósitos de matriz metálica à base níquel com adição de TaC e NbC produzidos via metalurgia do pó

Carbide reinforced metallic alloys potentially improve some important mechanical properties required for the overall use of important engineering materials such as steel and nickel. Nevertheless, improved performance is achieved not only by composition enhancement but also by adequate processing techniques, such as novel sintering methods in the case of powder metallurgy. The method minimizes energy losses in addition to providing uniform heating during sintering. Thus, the general objective of this study was to evaluate the density, hardness, flexural strength, dilatometric behavior and to analyze the microstructure of metal matrix composites based nickel with addition of carbides of tantalum and / or niobium when sintered in a conventional furnace and Plasma assisted debinding and sintering (PADS). Initially, were defineds best parameters of granulation, screening and mixing procedure. After, mixtures of carbonyl Ni and 5%, 10% and 15 wt.% NbC and TaC were prepared in a Y-type mixer under wet conditions during 60 minutes. The mixtures were then dried and granulated using 1.5 wt. % paraffin diluted in hexane. Granulates were cold pressed under 600 MPa. Paraffin was then removed from the pressed pellets during a pre-sintering process carried out in a tubular furnace at 500 °C during 30 min. The heating rate was 3 ºC/min. The pellets were then sintered using either a plasma assisted reactor or a conventional resistive tubular furnace. For both methods, the heating rate was set to 8 ºC/min up to 1150 °C. The holding time was 60 minutes. The microstructure of the sintered samples was evaluated by SEM. Brinell hardness tests were also carried out. The results revealed that higher density and higher hardness values were observed in the plasma-assisted sintered samples. Hardness increased with the concentration of carbides in the Ni-matrix. The flexural strength also increased by adding the carbides. The decline was larger for the sample with addition of 5% 5% TaC and NbC. In general, compositions containing added carbide 10% showed less porous and more uniform distribution of carbides in the nickel matrix microstructural appearance. Thus, both added carbide and plasma sintering improved density, hardness, flexural strength and microstructural appearance of the composites

Sistemas de automação e supervisão do laboratório de avaliação dos processos de medição de vazão e BSW

During a petroleum well production process, It is common the slmultaneous oil and water production, in proportion that can vary from 0% up to values close to 100% of water. Moreover, the production flows can vary a lot, depending on the charaeteristies of eaeh reservoir. Thus being, the meters used in field for the flow and BSW (water in the oil) measurement must work well in wide bands of operation. For the evaluation of the operation of these meters, in the different operation conditions, a Laboratory will be built in UFRN, that has for objective to evaluate in an automatic way the processes of flow and BSW petroleum measurement, considering different operation conditions. The good acting of these meters is fundamental for the accuracy of the measures of the volumes of production liquid and rude of petroleum. For the measurement of this production, the petroleum companies use meters that should indicate the values with tha largast possible accuracy and to respect a series of conditions and minimum requirements, estabelished by the united Entrance ANP/INMETRO 19106/2000. The laboratory of Evafuation of the Processes of Measurement of Flow and BSW to be built will possess an oil tank basically, a tank of water, besides a mixer, a tank auditor, a tank for separation and a tank of residues for discard of fluids, fundamental for the evaluation of the flow metars and BSW. The whole process will be automated through the use of a Programmable Logicat Controller (CLP) and of a supervisory system.This laboratory besides allowing the evaluation of flow meters and BSW used by petroleum companies, it will make possible the development of researches related to the automation. Besides, it will be a collaborating element to the development of the Computer Engineering and Automation Department, that it will propitiate the evolution of the faculty and discente, qualifying them for a job market in continuous growth. The present work describes the project of automation of the laboratory that will be built at of UFRN. The system will be automated using a Programmable Logical Controller and a supervisory system. The programming of PLC and the screens of the supervisory system were developed in this work

Estudo da hidrodinâmica de um novo separador líquido-líquido: aplicação ao sistema óleo-bruto/água produzida

This work aims to use a different hydrodynamic condition applied to a new design of mixer-settler on treating wastewater produced by petroleum industry, called MDIF (Misturador-Decantador à Inversão de Fases/ Mixer-Settler based on Phase Inversion MSPI). The use of this different hydrodynamic behaviour is possible due to vertical disposition of the device and the principle of Phase Inversion that controls the MDIF, providing the generation (creation) of a cascade of drops, into an organic layer, that works as micro-decanters, thus making possible the formation of a bed of non-coalesced drops, called Bed Formation . The use of this new hydrodynamics condition allows to increase the residence time of the oil carrier drops, into an organic layer, and the device can treat a greater volume of wastewater. In view of to get this condition it is necessary to operate at high throughput (58,6 m3.m-2.h-1). By results, the condition of Bed Formation is the best one to be used when MSPI operates with throughput up to 58,6 m3.m-2.h-1. The results using the condition of Bed Formation show that increasing the height of the bed of non-coalesced drops and/or decreasing the volumetric ratio (O/A) an increase of the separation efficiency is detected

Planejamento experimental aplicada a um novo separador líquido-líquido utilizado no tratamento de águas residuais contaminadas com petróleo

The present work had as objective to apply an experimental planning aiming at to improve the efficiency of separation of a new type of mixer-settler applied to treat waste water contaminated with oil. An unity in scale of laboratory, was installed in the Post-graduation Program of Chemical Engineering of UFRN. It was constructed in partnership with Petrobras S.A. This called device Misturador-Decantador a Inversão de Fases (MDIF) , possess features of conventional mixer-settler and spray column type. The equipment is composed of three main parts: mixing chamber; chamber of decantation and chamber of separation. The efficiency of separation is evaluated analyzing the oil concentrations in water in the feed and the output of the device. For the analysis one used the gravimetric method of oil and greases analysis (TOG). The system in study is a water of formation emulsified with oil. The used extractant is a mixture of Turpentine spirit hydro-carbons, supplied for Petrobras. It was applied, for otimization of the efficiency of separation of the equipment, an experimental planning of the composite central type, having as factorial portion fractionary factorial planning 2 5-2, with the magnifying of the type star and five replications in the central point. In this work, the following independents variables were studied: contents of oil in the feed of the device; volumetric ratio (O/A); total flowrate ; agitation in the mixing chamber and height of the organic bed. Minimum and maximum limits for the studied variables had been fixed according previous works. The analysis of variance for the equation of the empirical model, revealed statistically significant and useful results for predictions ends. The variance analysis also presented the distribution of the error as a normal distribution and was observed that as the dispersions do not depend on the levels of the factors, the independence assumption can be verified. The variation around the average is explained by 98.98%, or either, equal to the maximum value, being the smoothing of the model in relation to the experimental points of 0,98981. The results present a strong interaction between the variable oil contents in the feed and agitation in the mixing chamber, having great and positive influence in the separation efficiency. Another variable that presented a great positive influence was the height of the organic bed. The best results of separation efficiency had been obtained for high flowrates when associates the high oil concentrations and high agitation. The results of the present work had shown excellent agreement with the results carried out through previous works with the mixer-settler of phase inversion

Modelagem e simulação de um separador bifásico com inversão de fases induzida

The present work has the main goal to study the modeling and simulation of a biphasic separator with induced phase inversion, the MDIF, with the utilization of the finite differences method for the resolution of the partial differencial equations which describe the transport of contaminant s mass fraction inside the equipment s settling chamber. With this aim, was developed the deterministic differential model AMADDA, wich was admensionalizated and then semidiscretizated with the method of lines. The integration of the resultant system of ordinary differential equations was realized by means of a modified algorithm of the Adam-Bashfort- Moulton method, and the sthocastic optimization routine of Basin-Hopping was used in the model s parameter estimation procedure . With the aim to establish a comparative referential for the results obtained with the model AMADDA, were used experimental data presented in previous works of the MDIF s research group. The experimental data and those obtained with the model was assessed regarding its normality by means of the Shapiro-Wilk s test, and validated against the experimental results with the Student s t test and the Kruskal-Wallis s test, depending on the result. The results showed satisfactory performance of the model AMADDA in the evaluation of the MDIF s separation efficiency, being possible to determinate that at 1% significance level the calculated results are equivalent to those determinated experimentally in the reference works