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Se ha tratado de encontrar nuevas aplicaciones para el catalizador usado de las Unidades de F.C.C. de Refinerías (en adelante CUR).Dadas las características de este residuo industrial inerte (distribución granulométrica, superficie específica elevada y relación Si: Al en su composición), se ha estudiado la posibilidad de: a) utilizarlo como materia prima, sustituyendo al caolín en la fabricación de fritas cerámicas; b) emplearlo como materia prima, sustituyendo al caolín que se adiciona a las suspensiones acuosas de esmaltes cerámicos para mantener la estabilidad de las mismas o sustituyendo a Si y Al, en la formulación de los esmaltes; c) como material de partida para la obtención de zeolita 4A.En primer lugar, se han comparado las propiedades de los vidriados obtenidos a partir de cuatro fritas industriales diferentes y las características de los vidriados que resultan de aplicar fritas análogas, que se han preparado en el laboratorio, sustituyendo el caolín, presente en las materias primas de éstas, por CUR. Los resultados obtenidos han sido valorados positivamente.Posteriormente, utilizando CUR en vez de caolín, se preparó una de estas fritas, fundiéndola en un horno semi-industrial y aplicándola posteriormente. Los vidriados obtenidos presentaron también buenas cualidades técnicas y estéticas.A continuación, se han comparado las propiedades de los vidriados obtenidos con un esmalte industrial, que se emplea para obtener recubrimientos vidriados en piezas de pavimento cerámico, con las propiedades de los vidriados resultantes de sustituir, en la composición de dicho esmalte: a) el caolín por CUR; b) parte de la mezcla SiO2-Al2O3 por CUR. Los vidriados obtenidos tienen, en ambos casos, propiedades adecuadas para ser utilizados como recubrimiento en piezas de pavimento cerámico.Finalmente, se ha puesto a punto un procedimiento mediante el cual se puede obtener zeolita 4A, con un grado de cristalinidad superior al 90%, a partir de CUR. Este método, desarrollado a escala de laboratorio, se ha ensayado en planta piloto, habiéndose logrado unos excelentes resultados. La zeolita 4A obtenida posee una capacidad de intercambio iónico análoga a la de la zeolita 4A comercial y un índice de blancura y distribución de tamaño de partícula que se encuentran dentro del límite recomendado para utilizarla como aditivo (para la captación de iones Ca2+) en la fabricación de detergentes.

Ion exchange of heavy metals with zeolites is important in terms of different application areas. Industrial wastewater treatment and antibacterial applications are two essential areas that have taken great attention. While silver, zinc and copper are well known for their toxicity, they are also used as antibacterial agents in zeolites. The objective of this study is to investigate the single and multicomponent ion exchange behavior of zeolite 4A for silver, zinc, copper and sodium ions. For this purpose Ag+-Na+, Zn2+-Na+, Cu2+-Na+ binary systems and Ag+-Zn2+-Na+, Ag+-Cu2+-Na+, Cu2+-Zn2+-Na+ ternary systems were investigated in batch systems at 25&deg / C and 0.1 N. Binary ion exchange isotherms indicate that zeolite 4A has high selectivity for silver, zinc and copper with respect to sodium. All exchange isotherms lie above the diagonal over the whole range. Using the equilibrium data, the thermodynamic analysis of the binary systems were carried out. The thermodynamic equilibrium constants and the standard free energies of exchange were calculated as 340.9 and -14.5 kJ/mol for silver-sodium system, 40.5 and -4.6 kJ/mol for zinc-sodium system, and 161.2 and -6.3 kJ/mol for copper-sodium system, respectively. From these values, selectivity sequence of zeolite 4A was determined as Ag+ &gt / Cu2+ &gt / Zn2+. This selectivity sequence was also verified by the results of ternary ion exchange experiments. The experimental data were compared with the Langmuir and Freundlich isotherms. While Freundlich model gives a better correlation for Ag+-Na+ and Zn2+-Na+ exchange, Langmuir model represents a better fit to the experimental data of Cu2+-Na+ exchange.

In this study binary and ternary ion exchange on Zeolite NaA using silver and cadmium ions were investigated. Ion exchange were conducted at constant temperature (25oC) and normality (0.1N) in a batch system for both binary and ternary experiments. Zeolite weights were varied between 0.1 and 1 g for binary experiments. Thermodynamic analysis of binary ion exchange between Cd2+-Na+ and Ag+-Na+ were examined and thermodynamic equilibrium constant and Gibbs free energy were calculated. Thermodynamic equilibrium constants were found as respectively 28.2 and 300.4 for Cd2+-Na+ and Ag+-Na+ binary system. Standart free energy of Cd2+-Na+ and Ag+-Na+ binary exchange were calculated as -4.1 kJ/mol and -14.1 kJ/mol respectively. In literature Ay (2008) calculated the Gibbs free energy for Ag+-Na+ binary system as -14.4 kJ/mol and Biskup and Subotic (2010) and Gal et al. (1970) calculated the Gibbs free energy for Cd2+-Na+ binary system as -3.7 kJ/mol and -4.4 kJ/mol respectively. It is concluded Zeolite 4A has higher affinity to silver than cadmium and selectivity sequence was found as / Ag+&gt / Cd2+&gt / Na+. Langmuir and Freundlich isotherms were drawn to describe experimental data. As compared the R2 of isotherms, it is clearly seen that Freundlich isotherm provides better fit for Cd2+-Na+ binary ion exchange and Ag+-Na+ binary ion exchange. The ternary ion exchange isotherms were plotted using equivalent fraction of three ions (Ag+,Na+,Cd2+) which participated in ion exchange experiments to determine selectivity of zeolite 4A for cadmium and silver. Selectivity sequence was determined as Ag+ &gt / Cd2+ &gt / Na+ for ternary ion exchange.

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Mémoire numérisé par la Division de la gestion de documents et des archives de l'Université de Montréal.

Submitted by PPG Engenharia e Tecnologia de Materiais (engenharia.pg.materiais@pucrs.br) on 2018-05-03T11:34:42Z No. of bitstreams: 1 disserta??o Roger vers?o biblioteca.pdf: 9741593 bytes, checksum: 510807346e33704b6f1650648b1f1b19 (MD5) / Approved for entry into archive by Sheila Dias (sheila.dias@pucrs.br) on 2018-05-14T11:17:02Z (GMT) No. of bitstreams: 1 disserta??o Roger vers?o biblioteca.pdf: 9741593 bytes, checksum: 510807346e33704b6f1650648b1f1b19 (MD5) / Made available in DSpace on 2018-05-14T11:48:12Z (GMT). No. of bitstreams: 1 disserta??o Roger vers?o biblioteca.pdf: 9741593 bytes, checksum: 510807346e33704b6f1650648b1f1b19 (MD5) Previous issue date: 2018-01-15 / Developing technologies for the capture and geological storage of CO2 has been a constant challenge of the scientific community in the search for solutions that can reduce the environmental impacts caused by the release of this gas into the atmosphere. However, its storage in depleted oil wells has been shown to be a very important point, since the materials applied in wells can suffer degradation in the presence of CO2 in the supercritical state and at high pressures. The objective of this work is to evaluate the performance of the class G cement paste used in cementation of wellbore under conditions of geological carbon storage with replacement of part of the cement by pozoanic materials such as fly ash from the fossil fuel burning of the Candiota Thermoelectric Plant, and synthetic zeolites (4A-1 e 4A-2). The contents of the pozalanas used in substitution of the cement were 5% and 10% in weight. The medium in which samples were submitted for degradation tests was CO2 saturated water at 15 MPa pressure and 90 ?C for 7 and 14 days. Scanning Electron Microscopy (SEM), XRay Diffraction (XRD) and compressive strength tests were the characterization techniques used in this work. The results showed that the use of fly ash increased the compressive strength of the samples after 14 days, mainly for higher percentage of cement replacement by this material (10%), but its chemical degraded layer increased. In case of zeolites 4A-1 use, a lower compressive strength was observed compared to the standard paste, but the degraded layer was reduced. When zeolites 4A-2 were used significant loss of compressive strength was observed from 7 to 14 days, mainly for the proportion of the mixture of 10% and its degraded layer also reduced. / Desenvolver tecnologias para a captura e armazenamento geol?gico de CO2 tem sido um desafio constante da comunidade cient?fica na busca de solu??es que possam reduzir os impactos ambientais provocados pela libera??o desde g?s na atmosfera. Por?m, seu armazenamento em po?os depletados de petr?leo tem se mostrado o ponto mais desafiador, pois os materiais aplicados nestes po?os podem sofrer degrada??o na presen?a de CO2 em estado supercr?tico e em altas press?es. Este trabalho tem como objetivo avaliar o desempenho da pasta de cimento classe G, utilizada na cimenta??o e tamponamento dos po?os, em condi??es de armazenamento geol?gico de carbono com substitui??o de parte do cimento por materiais pozol?nicos. O material utilizado foi as cinzas volantes, oriundas da queima de carv?o mineral da Usina Termoel?trica de Candiota, e ze?litas 4A comerciais sint?ticas (4A-1 e 4A-2). Os teores utilizados das pozalanas em substitui??o ao cimento foram 5% e 10% em massa. O meio em que foram submetidas as amostras foi de ?gua saturada com CO2 a 15 MPa de press?o a 90? C por 7 e 14 dias. A Microscopia Eletr?nica de Varredura (MEV), a Difra??o de Raios X (DRX) e o teste de resist?ncia ? compress?o foram as t?cnicas de caracteriza??o utilizadas neste trabalho. Os resultados obtidos mostram que o uso de cinzas volantes aumentou aos 14 dias a resist?ncia ? compress?o das amostras, principalmente para maior a porcentagem de substitui??o do cimento por este material (10%), por?m a camada alterada quimicamente aumentou. Quando utilizadas as ze?litas 4A-1, notou-se uma menor resist?ncia ? compress?o que a pasta padr?o, mas a camada degradada reduziu. No caso das ze?litas 4A-2, foi constatada a perda significativa de resist?ncia ? compress?o dos 7 para 14 dias, principalmente para a amostra contendo 10% dessa zeolita, sendo que a camada alterada quimicamente tamb?m reduziu.

Mémoire numérisé par la Division de la gestion de documents et des archives de l'Université de Montréal

Gegenstand dieser Arbeit ist es, die Temperaturbeständigkeit von bikontinuierlichen Kompositmembranen bestehend aus Zeolith 4A und Visiomer HEMATMDI zu überprüfen und das Verhalten ihrer Permeanz im Verlauf der Temperaturerhöhung zu untersuchen. Weiterhin wird ihre Verwendbarkeit für technisch und industriell relevante Prozesse der Gastrocknung nachgewiesen. Zunächst wird thermogravimetrisch untersucht, bei welcher Temperatur Zersetzungserscheinungen an der polymeren Komponente auftreten. Anschließend wird thermogravimetrisch der Wassergehalt von Zeolith 4A im Bereich dieser Temperatur bestimmt. Hierauf folgen Permeationsmessungen mit Sauerstoff und Stickstoff an der bikontinuierlichen Kompositmembran. Die Temperatur wird hierbei schrittweise bis knapp unter die Zersetzungstemperatur des Polymers erhöht. Die Eignung der Membranen zur Gastrocknung wird exemplarisch an der Trocknung von Erdgas gezeigt. Es werden die Permeanzen für Wasserdampf und Methan als Hauptbestandteil von Erdgas mittels Einzelgasmessungen experimentell bestimmt. Aus diesen Permeanzen errechnet sich die ideale Selektivität der bikontinuierlichen Kompositmembran von Wasserdampf gegenüber Methan. Mit ihrer Hilfe lässt sich die Eignung der Membran zur Trocknung von Erdgas abschätzen. / The aim of this work is to study the temperature resistance of bicontinuous composite membranes, composed zeolite 4A and Visiomer HEMATMDI, and their permeances with rising temperatures. Furthermore their suitability for gas drying is investigated.