983 resultados para Refinery of YPF


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En el departamento Bermejo, provincia de Chaco, a fines del siglo XIX se origina uno de los ingenios azucareros más importantes del país: Las Palmas del Chaco Austral S.A. En la década de los noventa es víctima de las políticas de privatización imperantes del momento. Como consecuencia, se produce su cierre y posterior desaparición, lo que supuso la eliminación de la principal fuente de trabajo de la localidad. Las tendencias actuales y novedosas en teledetección, cartografía digital y Sistemas de Información Geográfica (SIG) son una forma útil e importante de ofrecer conocimientos actualizados para el diagnóstico, monitoreo y su aplicación en la gestión e investigación de recursos presentes en los distintos lugares de nuestro país. En el presente trabajo se pretende analizar los cambios producidos en el uso de suelo en las tierras del ex Ingenio a partir del cierre del mismo, mediante el uso de imágenes satelitales de los años 1987 y 2001, y de sistemas de información geográfica (SIG). El análisis multiespectral y multitemporal de las mismas permitirá discriminar los tipos de cobertura del suelo sobre la base de su respuesta espectral.

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La contaminación de suelos con hidrocarburos de petróleo en México es un problema que se ha vuelto muy común en nuestros días, debido principalmente a derrames, así como a las actividades propias de la industria petrolera. Algunos suelos contaminados, principalmente en el sureste de México, contienen concentraciones de hidrocarburos hasta de 450,000 mg/kg. Por dichas razones, una de las preocupaciones de las autoridades ambientales es el desarrollo de tecnologías eficientes y económicamente factibles que permitan la eliminación de este tipo de contaminantes. El saneamiento del sitio se puede lograr a través de diversos procedimientos, como son la aplicación de métodos físicos, químicos y biológicos (o combinaciones de ellas). La elección de un método depende de la naturaleza del contaminante, su estado físico, concentración, tipo de suelo, espacio físico disponible, tiempo destinado para su tratamiento, así como de los recursos económicos disponibles. Previa a la aplicación de la tecnología es necesario la realización de un diagnóstico de la contaminación del suelo, con el fin de conocer el tipo, concentración y distribución de los contaminantes presentes, así como el volumen de suelo a tratar, las condiciones climáticas de la zona, y características físicas del lugar (vías de acceso y servicios, entre otros). En la presente tesis, el empleo de surfactantes, se ha propuesto como una técnica para incrementar la movilidad de contaminantes orgánicos hidrofóbicos (HOCs) como hidrocarburos totales del petróleo (HTPs), bifenilos policlorados (PCBs), Benceno, Tolueno, Xilenos, explosivos, clorofenoles, pesticidas, entre otros, y así facilitar su degradación. Los surfactantes debido a que reducen la tensión superficial del agua, son moléculas formadas por grupos polares hidrofílicos y largas cadenas carbonadas hidrofóbicas. Sus grupos polares forman puentes hidrógeno con las moléculas de agua, mientras que las cadenas carbonadas se asocian a los hidrocarburos debido a interacciones hidrofóbicas que estos presentan. En soluciones acuosas, los surfactantes forman estructuras esféricas organizadas llamadas micelas. La solubilización de los contaminantes se lleva a cabo solamente cuando se forma la fase micelar, la cual se obtiene cuando la concentración del surfactante es superior a la concentración micelar crítica (CMC), es decir, arriba de la concentración de la cual el monómero se comienza a auto-agregar. La eficiencia de desorción de diésel por un surfactante depende de su naturaleza, de la dosis empleada, de la hidrofobicidad del contaminante, de la interacción surfactante-suelo y del tiempo de contacto surfactante-suelo. Sin embargo, la mejor eficiencia de desorción no está siempre relacionada con la mejor eficiencia de movilidad o solubilidad, debido principalmente a que el empleo de una alta concentración de surfactante puede inhibir la movilización. De acuerdo con información proporcionada por la Procuraduría Federal de Protección al Ambiente (PROFEPA), a la fecha no se ha llevado a cabo en México ninguna restauración de sitios específicamente contaminados con diésel, la técnica de lavado de suelos. Por lo anterior existe la necesidad de emplear la técnica de lavado de suelos ex situ. Específicamente en el suelo extraído de la ex refinería 18 de marzo ubicada en el Distrito Federal México y empleando una solución de surfactantes con agua desionizada, la cual consiste ponerlos en contacto con el suelo contaminado con diésel por medio de columnas de lavado cilíndricas, para lograr la remoción del contaminante. Se emplearon como surfactantes el lauril sulfato de sodio, lauril éter sulfato de sodio y Glucopon AV-100 a diferentes concentraciones de 0.5 a 4.0 [g/L], lográndose obtener una eficiencia del 80 % con este último surfactante. El lavado de suelos contaminados con diésel empleado surfactantes, es una tecnología que requiere que se profundice en el estudio de algunas variables como son el tipo de surfactante, concentración, tiempo de lavado, fenómenos de difusión, desorción, propiedades termodinámicas, entre otros. Los cuales determinarán el éxito o fracaso de la técnica empleada. Nowadays, soil pollution with oil in Mexico is a very common issue due mainly to both oil spill and oil activities. For example, mainly in the southeast area of Mexico, polluted soil contains high concentrations of hydrocarbons, up to 450,000 mg/kg. For these reasons, enviromental authorities have the concern in developing economically feasible and efficient technology that allow the elimination of these type of contaminants. The sanitation in sites can be achieved through several procedures such as physical, chemical and biological methods (or a combination among them). The choice of a method depends on the nature and physical state of the contaminant, the concentration, type of soil, physical space available, time consumption and financial resources. Before any technological application, a diagnostic of the polluted soil is necessary in order to know the type, concentration and distribution of contaminants as well as the soil volume, climatic conditions and physical features of the place (access routes and services, among others). In this thesis, surfactants has been proposed as a technique to increase the mobility of hydrophobic-organic contaminants (HOCs), e.g. total hydrocarbons of petroleum, polychlorinated biphenyls, benzene, toluene, xylenes, explosives, chlorophenols, pesticides, among others, and, hence, to facilitate degradation. Since surfactants reduce the water surface tension, they are molecules comprised of hydrophilic polar groups and long-hydrophobic carbon chains. Surfactant’s polar groups form hydrogen bonding with water molecules while carbon chains, i.e. hydrocarbon chains, have hydrophobic interactios. In aqueous solutions, surfactants form self-organised spherical structures called micelles. The solubilisation of contaminants is carried out only when the micellar phase is formed. This is obtained when the surfactant concentration is higher than the crítical micelle concentration (CMC), i.e. above the concentration where the surfactant monomer begins to self-aggregate. The diesel efficiency desorption by surfactants depends on their nature, the dose use, the contaminant hydrophobicity, the surfactant-soil interaction and the contact time with surfactant soil. However, the best desorption is not always related with the best either mobility or solubility efficiency since high concentration of surfactant can inhibit mobilisation. According to information of the Federal Bureau of Environmental Protection (PROFEPA), up today, there is not any restauration of diesel-polluted sites using the washing-soil technique. Due to the above, there exist the necessity of employing the waching-soil technique ex situ. More specifically, a sample soil from the oil-refinery of “18 de marzo” in Mexico city was extracted and a surfactant solution with deionised water was put in contact with the diesel contaminated soil by means of cylindrical waching columns in order to remove the contaminant. The surfactants employed in this work were sodium lauryl sulfate, sodium lauryl ether sulfate and Glucopon AV-100 at different concentrations of 0.5 to 4 [g/L], obtaining a efficiency of 80 % with this last surfactant. The washing of diesel-polluted soil using surfactants is a technology which requires a deeper study of some variables such as the type of surfactant, concentration, washing time, difusión phenomena, desorption, thermodynamic properties, among others. These parameters determine the succes or failure of the employed technique.

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The presence of calcium hydroxide (Ca(OH)2) in Bayer residue slurry inhibits the effectiveness of the seawater neutralisation process to reduce the pH and aluminium concentration in the residue. An increase in the slurry pH (reversion), after seawater neutralisation, is caused by the dissolution of calcium hydroxide and hydrocalumite (solid components found in bauxite refinery residue). Reversion was not observed when the final solution pH was greater than 10.5, due to hydrocalumite being in a state of equilibrium at high pH. Hydrocalumite has been found to form during the neutralisation process when high concentrations of calcium hydroxide are present in the residue liquor. The dissolution of hydrocalumite releases hydroxyl (OH-) and aluminium ions back into solution after the seawater neutralisation (SWN) process, which causes pH and aluminium reversion to occur. This investigation looks at the effect of Ca(OH)2 and subsequently hydrocalumite on the pH and aluminium concentration in bauxite refinery residue liquors after the SWN process.

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Bauxite refinery residues (red mud) are derived from the Bayer process by the digestion of crushed bauxite in concentrated sodium hydroxide at elevated temperatures and pressures. This slurry residue, if untreated, is unsuitable for discharge directly into the environment and is usually stored in tailing dams. The liquid portion has the potential for discharge, but requires pre-treatment before this can occur. The seawater neutralisation treatment facilitates a significant reduction in pH and dissolved metal concentrations, through the precipitation of hydrotalcite-like compounds and some other Mg, Ca, and Al hydroxide and carbonate minerals. The hydrotalcite-like compounds, precipitated during seawater neutralisation, also remove a range of transition metals, oxy-anions and other anionic species through a combination of intercalation and adsorption reactions: smaller anions are intercalated into the hydrotalcite matrix, while larger molecules are adsorbed on the particle surfaces. A phenomenon known as ‘reversion’ can occur if the seawater neutralisation process is not properly controlled. Reversion causes an increase in the pH and dissolved impurity levels of the neutralised effluent, rendering it unsuitable for discharge. It is believed that slow dissolution of components of the red mud residue and compounds formed during the neutralisation process are responsible for reversion. This investigation looked at characterising natural hydrotalcite (Mg6Al2(OH)16(CO3)∙4H2O) and ‘Bayer’ hydrotalcite (synthesised using the seawater neutralisation process) using a variety of techniques including X-ray diffraction, infrared and Raman spectroscopy, and thermogravimetric analysis. This investigation showed that Bayer hydrotalcite is comprised of a mixture of 3:1 and 4:1 hydrotalcite structures and exhibited similar chemical characteristic to the 4:1 synthetic hydrotalcite. Hydrotalcite formed from the seawater neutralisation of Bauxite refinery residues has been found not to cause reversion. Other components in red mud were investigated to determine the cause of reversion and this investigation found three components that contributed to reversion: 1) tricalcium aluminate, 2) hydrocalumite and 3) calcium hydroxide. Increasing the amount of magnesium in the neutralisation process has been found to be successful in reducing reversion.

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This investigation has shown that by transforming free caustic in red mud (RM) to Bayer hydrotalcite (during the seawater neutralization (SWN) process) enables a more controlled release mechanism for the neutralization of acid sulfate soils. The formation of hydrotalcite has been confirmed by X-ray diffraction (XRD) and differential thermalgravimetric analysis (DTG), while the dissolution of hydrotalcite and sodalite has been observed through XRD, DTG, pH plots, and ICP-OES. Coupling of all techniques enabled three neutralization mechanisms to be determined: (1) free alkali, (2) hydrotalcite dissolution, and (3) sodalite dissolution. The mechanisms are determined on the basis of ICP-OES and kinetic information. When the mass of RM or SWN-RM is greater than 0.08 g/50 mL, the pH of solution increases to a suitable value for plant life with aluminum leaching kept at a minimum. To obtain a neutralization pH greater than 6 in 10 min, the following ratio of bauxite residue (g) in 50 mL with a known iron sulfate (Fe2(SO4)3) concentration can be determined as follows: 0.04 g:50 mL:0.1 g/L of Fe2(SO4)3.

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This investigation has demonstrated the need for thermal treatment of seawater neutralised red mud (SWRM) in order to obtain reasonable adsorption of Reactive Blue dye 19 (RB 19). Thermal treatment results in a greater surface area, which results in an increased adsorption capacity due to more available adsorption sites. Adsorption of RB 19 has been found to be best achieved in acidic conditions using SWNRM400 (heated to 400 �C) with an adsorption capacity of 416.7 mg/g compared to 250.0 mg/g for untreated SWNRM. Kinetic studies indicate a pseudosecond-order reaction mechanism is responsible for the adsorption of RB 19 using SWNRM, which indicates adsorption occurs by electrostatic interactions.

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Tricalcium aluminate, hydrocalumite and residual lime have been identified as reversion contributing compounds after the seawater neutralisation of bauxite refinery residues. The formation of these compounds during the neutralisation process is dependent on the concentration of residual lime, pH and aluminate concentrations in the residue slurry. Therefore, the effect of calcium hydroxide (CaOH2) in bauxite refinery liquors was analysed and the degree of reversion monitored. This investigation found that the dissolution of tricalcium aluminate, hydrocalumite and CaOH2 caused reversion and continued to increase the pH of the neutralised residue until a state of equilibrium was reached at a solution pH of 10.5. The dissolution mechanism for each compound has been described and used to demonstrate the implications that this has on reversion in seawater neutralised Bayer liquor. This investigation describes the limiting factors for the dissolution and formation of these trigger compounds as well as confirming the formation of Bayer hydrotalcite (mixture of Mg6Al2(OH)16(CO32-,SO42-)•xH2O and Mg8Al2(OH)12(CO32-,SO42-)•xH2O) as the primary mechanism for reducing reversion during the neutralisation process. This knowledge then allowed for a simple but effective method (addition of magnesium chloride or increased seawater to Bayer liquor ratio) to be devised to reduce reversion occurring after the neutralisation of Bayer liquors. Both methods utilise the formation of Bayer hydrotalcite to permanently (stable in neutralised residue) remove hydroxyl (OH-) and aluminate (Al(OH)4-) ions from solution.

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The farm production of silage as a winter-feed supplement is widespread. However, the bins in which silage is produced are subject to acidic and microbial attacks. Both these types of attack can lead to a weakening and failure of the concretes, especially on the outer lip of the open side of the silage pit. Consequently, the development of an acid-resistant concrete that can extend the life span of silage bins on farms could lead to considerable cost savings for farmers and, hence, can improve farm productivity. This paper reports on test results of an investigation into the behaviour of concrete containing seawater-neutralised bauxite refinery residues (Bauxsol™) exposed to sulphuric acid environments in the laboratory and to silage effluents. The concrete manufactured had a fixed water–cement ratio of 0.55 and natural sand was replaced with the Bauxsol™ at 0%, 5%, 10%, 15% and 20% by cement mass. Results indicated that the use of Bauxsol™ as a sand replacement material improved the behaviour of concrete both in sulphuric acid in the laboratory as well as in the silage effluent. Consequently, it is concluded that the Bauxsol™ can be used to replace 10% of natural sand to produce concrete that is resistant to silage effluents, providing an extended service life over conventional concretes used in silage pits.

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Various industrial by-products, such as fly ash, ground granulated blast-furnace slag and silica fume, have been used in concrete to improve its properties. This also enables any environmental issues associated with their disposal. Another material that is available in large quantities and requiring alternative methods of disposal is the Bauxite Refinery Reside (BRR) from the Bayer process used to extract alumina from bauxite. As this is highly caustic and causes many health hazards, Virotec International Ltd. developed a patented technology to convert this into a material that can be used commercially, known as Bauxsol™, for various environmental remediation applications. This use is limited to small quantities of seawater-neutralised BRR and hence an investigation was carried out to establish its potential utilisation as a sand replacement material in concrete. In addition to fresh properties of concrete containing seawater-neutralised BRR up to 20% by mass of Portland cement, mechanical and durability properties were determined. These properties indicated that seawater-neutralised BRR can be used to replace natural sand up to 10% by mass of cement to improve the durability properties of concrete without detrimentally affecting their physical properties. Combining these beneficial effects with environmental remediation applications, it can be concluded that there are specific applications where concretes containing seawater-neutralised BRR could be used.