Modelagem e simulação de um sistema de bombeio mecânico em poços direcionais utilizando parâmetros concentrados

This work aims presenting the development of a model and computer simulation of a sucker rod pumping system. This system take into account the well geometry, the flow through the tubing, the dynamic behavior of the rod string and the use of a induction motor model. The rod string were modeled using concentrated parameters, allowing the use of ordinary differential equations systems to simulate it s behavior

Estudo de estratégias de otimização para poços de petróleo com elevação por bombeio de cavidades progressivas

The progressing cavity pump artificial lift system, PCP, is a main lift system used in oil production industry. As this artificial lift application grows the knowledge of it s dynamics behavior, the application of automatic control and the developing of equipment selection design specialist systems are more useful. This work presents tools for dynamic analysis, control technics and a specialist system for selecting lift equipments for this artificial lift technology. The PCP artificial lift system consists of a progressing cavity pump installed downhole in the production tubing edge. The pump consists of two parts, a stator and a rotor, and is set in motion by the rotation of the rotor transmitted through a rod string installed in the tubing. The surface equipment generates and transmits the rotation to the rod string. First, is presented the developing of a complete mathematical dynamic model of PCP system. This model is simplified for use in several conditions, including steady state for sizing PCP equipments, like pump, rod string and drive head. This model is used to implement a computer simulator able to help in system analysis and to operates as a well with a controller and allows testing and developing of control algorithms. The next developing applies control technics to PCP system to optimize pumping velocity to achieve productivity and durability of downhole components. The mathematical model is linearized to apply conventional control technics including observability and controllability of the system and develop design rules for PI controller. Stability conditions are stated for operation point of the system. A fuzzy rule-based control system are developed from a PI controller using a inference machine based on Mandami operators. The fuzzy logic is applied to develop a specialist system that selects PCP equipments too. The developed technics to simulate and the linearized model was used in an actual well where a control system is installed. This control system consists of a pump intake pressure sensor, an industrial controller and a variable speed drive. The PI control was applied and fuzzy controller was applied to optimize simulated and actual well operation and the results was compared. The simulated and actual open loop response was compared to validate simulation. A case study was accomplished to validate equipment selection specialist system

Desenvolvimento de um simulador de bombeio por cavidades progressivas

The method of artificial lift of progressing cavity pump is very efficient in the production of oils with high viscosity and oils that carry a great amount of sand. This characteristic converted this lift method into the second most useful one in oil fields production. As it grows the number of its applications it also increases the necessity to dominate its work in a way to define it the best operational set point. To contribute to the knowledge of the operational method of artificial lift of progressing cavity pump, this work intends to develop a computational simulator for oil wells equipped with an artificial lift system. The computational simulator of the system will be able to represent its dynamic behavior when submitted to the various operational conditions. The system was divided into five subsystems: induction motor, multiphase flows into production tubing, rod string, progressing cavity pump and annular tubing-casing. The modeling and simulation of each subsystem permitted to evaluate the dynamic characteristics that defined the criteria connections. With the connections of the subsystems it was possible to obtain the dynamic characteristics of the most important arrays belonging to the system, such as: pressure discharge, pressure intake, pumping rate, rod string rotation and torque applied to polish string. The shown results added to a friendly graphical interface converted the PCP simulator in a great potential tool with a didactic characteristic in serving the technical capability for the system operators and also permitting the production engineering to achieve a more detail analysis of the dynamic operational oil wells equipped with the progressing cavity pump

Modelagem dinâmica do escoamento de um sistema de elevação por plunger lift

A critical problem in mature gas wells is the liquid loading. As the reservoir pressure decreases, gas superficial velocities decreases and the drag exerted on the liquid phase may become insufficient to bring all the liquid to the surface. Liquid starts to drain downward, flooding the well and increasing the backpressure which decreases the gas superficial velocity and so on. A popular method to remedy this problem is the Plunger Lift. This method consists of dropping the "plunger"to the bottom of the tubing well with the main production valve closed. When the plunger reaches the well bottom the production valve is opened and the plunger carry the liquid to the surface. However, models presented in literature for predicting the behavior in plunger lift are simplistic, in many cases static (not considering the transient effects). Therefore work presents the development and validation of a numerical algorithm to solve one-dimensional compressible in gas wells using the Finite Volume Method and PRIME techniques for treating coupling of pressure and velocity fields. The code will be then used to develop a dynamic model for the plunger lift which includes the transient compressible flow within the well

Incrustação em poço produtor de petróleo e gás natural: um estudo de caso

Water and gas is a common by - product of the oil production process. Production may be compromised by the precipitation of inorganic salts in both the reservoir and producing well, through scale formation. This precipitation is likely the cause of the formation damage. High temperatures and h igh pressures (HTHP) may favor the precipitation of insoluble salts. The most common types of scale in oil fields are calcium carbonate and calcium sulphate, strontium and barium sulphate. New types of scale formation have attracted special attention such as zinc sulphide and lead. This precipitation may occur in the pores of reservoir rocks, in the production string and in equipment, causing obstructions and consequent production losses. In this study, the influence of well depth on incrustation compositio n was investigated to design removal treatments and assess the behavior of these deposits along the string, through the analysis of pressure and temperature. Scale residues were recovered from the inside of the production string of an oil and gas well duri ng the string removal operation. A total of 10 samples from different depths (15.4 m to 4061.5 m) were obtained. Initially a dissolution test was conducted in weak acid, similar to that used in removal operations with this type of scale formation. Majority composition was defined and confirmed by dissolution tests using X - Ray Fluorescence Spectroscopy (XRF), X - Ray Diffraction (XRD) and Scanning Electron Microscope (SEM) techniques. Residues with distinct characteristics were observed in different proportion s, showing a tendency toward increased and/or decreased mass with depth. In the samples closest to the surface, typical sandstone residues were found, with calcium (45% Ca) as the metal of highest concentration. The obtained results indicate correlations o f the scale types studied with the depth and, consequently, with the thermodynamic conditions of pressure and temperature.

Modelagem e simulação de um sistema de bombeio mecânico em poços direcionais utilizando parâmetros concentrados

This work aims presenting the development of a model and computer simulation of a sucker rod pumping system. This system take into account the well geometry, the flow through the tubing, the dynamic behavior of the rod string and the use of a induction motor model. The rod string were modeled using concentrated parameters, allowing the use of ordinary differential equations systems to simulate it s behavior

Determinação de fósforo orgânico em águas de produção petrolífera por ICP- AES e ICP- MS após pré-concentração em coluna de sílica-C18

Results on the optimization of analytical methods for the determination of phosphorus in phosphino-polycarboxylate (PPCA), used frequently as scale inhibitor during oil production, by ICP-AES and ICP-MS are presented. Due to the complex matrix of production waters (brines) and their high concentration in inorganic phosphorus, the separation of organic phosphorus prior to its determination is necessary. In this work, minicolumns of silica immobilized C18 were used. Optimization of the separation step resulted in the following working conditions: (1) prewashing of the column with methanol (80% v/v); (2) use of a flow rate of 5 mL/min and 10 mL/min, respectively, for the preconditioning step and for percolation of the water sample; (3) final elution of organic phosphorus with 7 mL of buffer of H3BO3/NaOH (0.05 M, pH 9) with a flow rate of 1 mL/min. Sample detection limits (3s) for different combinations of nebulizers and spectrometric methods, based on 10 mL water aliquots, are: ICP-AES -Cross flow (47 mg/L) and Ultrasonic (18 mug/L); ICP-MS -Cross flow (1.2 mug/L), Cyclonic (0.7 mug/L) and Ultrasonic (0.5 mug/L). Typical recoveries of organic phosphorus are between 90 and 95% and the repeatability of the whole procedure is better than 10%. The developed methodology was applied successfully to samples from the oil-well NA 46, platform PNA 2, Campos basin, Brazil. Assessment of the PPCA inhibitor was possible at lower concentrations than achieved by current analytical methods, resulting in benefits such as reduced cost of chemicals, postponed oil production and lower environmental impacts.

Remoção de óleo da água de produção por flotação em coluna utilizando tensoativos de origem vegetal

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.

Utilização de uma coluna de flotação para remoção de compostos orgânicos da água de produção

Innovative technologies using surfactant materials have applicability in several industrial fields, including petroleum and gas areas. This study seeks to investigate the use of a surfactant derived from coconut oil (SCO saponified coconut oil) in the recovery process of organic compounds that are present in oily effluents from petroleum industry. For this end, experiments were accomplished in a column of small dimension objectifying to verify the influence of the surfactant SCO in the efficiency of oil removal. This way, they were prepared emulsions with amount it fastens of oil (50, 100, 200 and 400 ppm), being determined the great concentrations of surfactant for each one of them. Some rehearsals were still accomplished with produced water of the industry of the petroleum to compare the result with the one of the emulsions. According to the experiments, it was verified that an increase of the surfactant concentration does not implicate in a greater oil removal. The separation process use gaseous bubbles formed when a gas stream pass a liquid column, when low surfactant concentrations are used, it occurs the coalescence of the dispersed oil droplets and their transport to the top of the column, forming a new continuous phase. Such surfactants lead to a gas-liquid interface saturation, depending on the used surfactant concentration, affecting the flotation process and influencing in the removal capacity of the oily dispersed phase. A porous plate filter, with pore size varying from 40 to 250 mm, was placed at the base of the column to allow a hydrodynamic stable operation. During the experimental procedures, the operating volume of phase liquid was held constant and the rate of air flow varied in each experiment. The resulting experimental of the study hydrodynamic demonstrated what the capturing of the oil was influenced by diameter of the bubbles and air flow. With the increase flow of 300 about to 900 cm3.min-1, occurred an increase in the removal of oil phase of 44% about to 66% and the removal kinetic of oil was defined as a reaction of 1° order

Utilização de uma coluna de flotação para remoção de compostos orgânicos da água de produção

Innovative technologies using surfactant materials have applicability in several industrial fields, including petroleum and gas areas. This study seeks to investigate the use of a surfactant derived from coconut oil (SCO saponified coconut oil) in the recovery process of organic compounds that are present in oily effluents from petroleum industry. For this end, experiments were accomplished in a column of small dimension objectifying to verify the influence of the surfactant SCO in the efficiency of oil removal. This way, they were prepared emulsions with amount it fastens of oil (50, 100, 200 and 400 ppm), being determined the great concentrations of surfactant for each one of them. Some rehearsals were still accomplished with produced water of the industry of the petroleum to compare the result with the one of the emulsions. According to the experiments, it was verified that an increase of the surfactant concentration does not implicate in a greater oil removal. The separation process use gaseous bubbles formed when a gas stream pass a liquid column, when low surfactant concentrations are used, it occurs the coalescence of the dispersed oil droplets and their transport to the top of the column, forming a new continuous phase. Such surfactants lead to a gas-liquid interface saturation, depending on the used surfactant concentration, affecting the flotation process and influencing in the removal capacity of the oily dispersed phase. A porous plate filter, with pore size varying from 40 to 250 mm, was placed at the base of the column to allow a hydrodynamic stable operation. During the experimental procedures, the operating volume of phase liquid was held constant and the rate of air flow varied in each experiment. The resulting experimental of the study hydrodynamic demonstrated what the capturing of the oil was influenced by diameter of the bubbles and air flow. With the increase flow of 300 about to 900 cm3.min-1, occurred an increase in the removal of oil phase of 44% about to 66% and the removal kinetic of oil was defined as a reaction of 1° order.

Maximização da produção de paraxileno

Pretendeu-se, com o presente trabalho, efectuar um estudo sobre a possibilidade de aumentar a produção de paraxileno na unidade processual existente na refinaria da Galp no Porto. Foram estudados o conjunto de colunas T-0306 e T-0307 e a coluna T-0303, recorrendo ao uso do AspenPlus, na realização da simulação do processo nas condições actuais e para a realização da análise de sensibilidade, que permitiu verificar se o equipamento existente possui capacidade para satisfazer as necessidades exigidas pelo processo quando se pretende aumentar a produção. Com a simulação do processo, foi verificado que este já se encontra a laborar em condições óptimas. Na realização da análise de sensibilidade foram variados para o conjunto T-0306 e T- 0307, o caudal de alimentação entre 62780 e 95000 kg/h, o caudal de destilado da T-0306 entre 15833 e 23911 kg/h e o caudal de destilado da T-0307 entre 139 e os 235 kg/h. No caso da T-0303, foi variado o caudal de refinado entre 201240 e 304600 kg/h, o caudal de destilado e o caudal da corrente lateral, variam entre 77290 a 116930 kg/h. Pretendeu-se obter soluções que conseguissem cumprir as especificações relativas aos produtos obtidos, nomeadamente paraxileno com uma pureza de 99,6% e uma recuperação de 99%, tolueno com uma pureza de 97% e uma recuperação de 90% (T-0306 e T-0307). No caso da T- 0303, obter paraxileno com uma pureza de 2,23% e paradietilbenzeno com uma pureza de 99,0% e ambos com uma recuperação de 99%. Para as simulações que cumpriram as especificações anteriores, verificou-se se a energia transferida em aeroarrefecedores, fornalhas e permutadores excedem em 25% o seu valor de projecto. Em caso afirmativo isso significou o acréscimo de uma peça de equipamento idêntica à existente. A análise de sensibilidade permitiu concluir a separação é possível para os caudais actuais de extracto e refinado e para um aumento destes de 32, 40 e 50%. Foi ainda possível concluir que para os caudais actuais é necessária a colocação de novos aeroarrefecedores para as colunas T-0306 e T-0303 e de uma nova fornalha para a coluna T-0303. Para um aumento dos caudais de 32% para além das alterações referidas anteriormente é necessária a colocação de um novo aeroarrefecedor na coluna T-0307 e de uma nova fornalha da coluna T-0306. Se aumentarmos os caudais em 40% será também necessário o acréscimo de permutadores para a coluna T-0307. Para o aumento de 50%, os calores de permuta são excedidos em bastante mais do que 25%, em todos os aeroarrefecedores, permutadores e fornalhas. Uma vez que todas as colunas se encontram a funcionar acima da sua capacidade, concluiu-se que em ambos os casos seria necessária a montagem de uma segunda linha em paralelo e igual à existente. Implicando com esta alteração um investimento total de 10.439.574,36€.

Simulação da produção de Paraxileno

O trabalho tem como objectivo a simulação e verificação do funcionamento de 3 colunas de destilação, a T-0303, a T-0306 e a T-0307, integrantes do processo de produção de p-xileno, baseado nos dados relativos ao ano de 2008, existente na refinaria da Galp no Porto. A abordagem consistiu em utilizar o AspenPlus quer para a simulação quer para a optimização, sendo esta última complementada com um planeamento experimental e optimização no Minitab15. O critério de optimização foi estabelecido a partir de uma análise ao processo actual, na qual se averiguou que se poderia, no limite: produzir mais 15,30ton.ano-1 de p-xileno no conjunto de colunas T-0306 e T-0307; remover mais 1,36ton.ano-1 de dessorvente na coluna T-0303 e diminuir a energia necessária para o processo. Da optimização à coluna T-0303, obteve-se uma melhoria de remoção de 0,34ton.ano-1 de dessorvente, e uma diminuição na energia necessária para 333,24.106kWh por ano. Para obter esta optimização houve necessidade de ultrapassar em 109,852kW a potência da bomba P0306A/S e alterou-se a razão de refluxo na base para 46,1. A optimização conjunta das colunas T-0306 e T-0307 apenas possibilita uma melhoria de p-xileno de 3,4ton.ano-1. De uma optimização individual da coluna T-0307, mantendo a coluna T-0306 nas condições actuais, obteve-se uma melhoria na produção de p-xileno de 14,62ton.ano-1. Neste ensaio as potências do condensador E-0314, do reebulidor E-0306 e da bomba P0314A/S excedem, as actuais em, respectivamente, 35,71kW, 35,74kW e 0,12kW. Enquanto para a situação actual o custo de p-xileno equivale a 722,17€.ton-1, para a optimização simultânea da coluna T-0303 e T-0307, é de 723,39€.ton-1 e para a optimização de apenas da coluna T-0307 é de 722,81€.ton-1. Perante um preço de venda actual de pxileno de 749,10€.ton-1 todas as situações são favoráveis. Em suma, é possível uma optimização processual mas o custo por tonelada de pxileno fica superior ao actual.

Simulação da secção de recuperação de solvente do processo de produção do PEAD

A presente dissertação foi realizada no âmbito de um estágio curricular no complexo petroquímico da Repsol Polímeros em Sines e teve como objectivo implementar uma simulação da secção de recuperação de solvente da unidade de produção de PEAD. A simulação foi realizada através do software Aspen Hysys (v. 7.3) e posteriormente validada, onde se verificou uma boa correspondência entre o comportamento simulado e o do processo industrial. Após validação, com o intuito de analisar a resposta do sistema a alterações processuais, foram elaborados dois casos de estudo: Alteração do comonómero para 1-hexeno e substituição do n-hexano para n-pentano como solvente. No primeiro caso de estudo foram encontrados problemas na purificação do solvente. A separação da mistura n-hexano/1-hexeno foi estudada por destilação convencional e extractiva (com adição de n-metil-2-pirrolidona). Por destilação convencional não foi possível separar completamente os dois compostos, mas foi conseguida a condição mínima requerida pelas limitações do processo, de um caudal de 10 ton/h de hexano na corrente de topo, juntamente com os 700 kg/h de comonómero, com uma coluna a operar a 110 kPa, com 130 pratos e cuja alimentação entrava no 5º andar. A destilação extractiva revelou-se o método mais eficaz, conseguindo-se separar completamente as duas espécies através de uma coluna de destilação com 10 pratos a 110 kPa com a alimentação e solvente a entrar respectivamente no 4º e 5º andar. Para remoção do agente extractivo, cada uma das correntes sofre outra destilação. No segundo caso de estudo verificou-se que a secção simulada com pentano apresenta temperaturas de operação inferiores, o que por um lado vai diminuir o consumo de vapor de média e de alta pressão, mas por outro aumenta a 47992% a utilização de brine. Desta forma, atendendo ao custo elevado desta utilidade, a substituição não apresenta clara vantagem energética ao processo.

Simulação e otimização da coluna de vácuo II da refinaria de Sines

O trabalho realizado foi desenvolvido no âmbito de um estágio curricular de seis meses realizado na Refinaria de Sines da Galp Energia. O principal objetivo foi a otimização da maior coluna de destilação de vácuo existente, uma vez que com o início do funcionamento de novas unidades, como é o caso do Hydrocraker, a produção de gasóleo de vácuo na Refinaria não é suficiente para assegurar a carga das unidades sendo necessário importar, diminuindo assim as margens das unidades. Foi implementada a simulação da coluna de destilação de vácuo II em ASPEN PLUS® para o caso de design, usando as condições de operação que o licenciador usou nas suas simulações para o re-vamping da unidade. Posteriormente foi efetuada a implementação para o caso de Test Run, em que são verificadas as produções projetadas para a coluna, e foram implementados na coluna 4 casos de operação real, onde foram recolhidos os dados de operação e comparadas as características dos produtos simulados com os resultados obtidos nos ensaios das amostras efetuados pelo Laboratório. No caso de design verifica-se que o modelo representa de forma aceitável as características dos pro-dutos extraídos. Tanto para o caso de Test Run como para os casos reais verifica-se que o modelo representa, na maioria dos casos, as características do destilado e do HVGO nas partes finais das destilações destes produtos, enquanto que o modelo representa as características do LVGO na fase inicial da destilação. Para otimização da coluna de vácuo verificou-se que os parâmetros com maior influência na produção de gasóleo de vácuo são a temperatura da zona de flash da coluna e o caudal de vapor de stripping introduzido no fundo da coluna.

Produção de cachos e parâmetros genéticos de híbridos de caiaué com dendezeiro

O objetivo deste trabalho foi avaliar a produção de cachos e estimar os parâmetros genéticos de progênies F1 de caiaué (Elaeis oleifera) com dendezeiro (E. guineenses). As progênies foram plantadas em parcelas com número variável de plantas. Avaliaram-se número (NC), peso médio (PMC) e peso total de cachos (PTC) por planta, do sétimo ao décimo-terceiro ano após o plantio. Estes dados foram analisados por REML/BLUP em 59 progênies, com delineamento desbalanceado em linha e coluna. Todos os caracteres apresentaram considerável variabilidade, com coeficientes de variação genética entre 18,1 e 25,5%, quanto à progênie, e de 25,6 a 36,0% quanto a indivíduo. Pela seleção das cinco melhores progênies, podem ser obtidos ganhos superiores a 30%, para NC e PTC, e acima de 20% para PMC; e, com a seleção dos cinco melhores indivíduos, ganhos acima de 65%, para NC e PTC, e acima de 60% para PMC. As progênies apresentam alta variabilidade genética quanto à produção de cachos. Ganhos genéticos elevados podem ser obtidos pela seleção tanto de indivíduos para clonagem quanto de progênies para reprodução sexuada.