The goal of this project was to understand and model the performance of hybrid inorganic-organic membranes under realistic operating conditions for hydrocarbon gas/vapor separation, using butane isomers as the model vapors and a hybrid membrane of 6FDA-DAM-5A as an advanced separation system. To achieve the set goal, three objectives were laid out. The first objective was to determine the factors affecting separation performance in dense neat polymer. One main concern was plasticization. High temperature annealing has been reported as an effect means of suppressing plasticization. A study on the effect of annealing temperature was performed by analyzing data acquired via sorption and permeation measurements. Based on the findings from this study, a suitable annealing temperature was determined. Another factor studied was the effect of operating temperature. In deciding a suitable operating temperature, factors such as its possible effect on plasticization as well as reducing heating/cooling cost in industrial application were considered. Based on the knowledge that industrial applications of this membrane would involve mixture separation, the second objective was to understand and model the complexity of a mixed gas system. This was investigated via permeation measurements using three feed compositions. An interesting transport behavior was observed in the mixed gas system, which to the best of our knowledge, has not been observed in other mixed gas systems involving smaller penetrants. This mixed gas transport behavior presented a challenge in predictability using well-established transport models. Two hypotheses were made to explain the observed transport behavior, which led to the development of a new model termed the HHF model and the introduction of a fitting parameter termed the CAUFFV fit. Both the HHF model and CAUFFV fit showed better agreement with experimental data than the well-established mixed gas transport model. The final objective was to explore the use of mixed matrix membranes as a means of improving the separation performance of this system. A major challenge with the fabrication of good mixed matrix membranes was the adhesion of the zeolite particle with the polymer. This was addressed via sieve surface modification through a Grignard treatment process. Although a Grignard treatment procedure existed, there was a challenge of reproducibility of the treatment. This challenge was addressed by exploring the relationship between the sieves and the solvent used in the treatment, and taking advantage of this relationship in the Grignard treatment process. This study helped identify a suitable solvent, which allowed for successful and reproducible treatment of commercial LTA sieves; however, treatment of lab-made sieves continues to prove challenging. Based on improved understanding of the Grignard treatment reaction mechanism, modifications were made to the existing Grignard treatment procedure, resulting in the introduction of a "simplified" Grignard treatment procedure. The new procedure requires less control over the reaction process, thus making it more attractive for industrial application. Permeation measurements were made using mixed matrix membranes in both single and mixed gas systems. Selectivity enhancements were observed under both single and mixed gas systems using sieve loadings of 25 and 30wt%. The Maxwell model was used to make predictions of mixed matrix membrane performance. Although the experimental results were not in exact agreement with Maxwell predictions, the observed selectivity enhancement was very encouraging and shows potential for future application. Recommendations were made for future study of this system.

Poly(ether-b-amide) (Pebax® grade 1074) is a waterproof breathable block copolymer containing soft poly(ethylene oxide) and rigid polyamide 12 segments. Its intrinsic gas permeabilities to nitrogen, oxygen, methane, helium, hydrogen, and carbon dioxide were tested under different feed pressures (0.3 – 2.5 MPa) and temperatures (20 – 80 °C). This helps to obtain a comprehensive understanding of the polymer, because prior work reported in the literature addressed only a few gases and used inconsistent membrane preparation and test methods. Relatively high polar (or quadrupolar)/nonpolar gas selectivity were observed. CO2/N2 selectivity was demonstrated to be as high as 105±0.4 in Pebax®1074, with CO2 permeability coefficient of approximately 180±1 Barrer at room temperature. Additionally, the effects of solvent used in membrane preparation, heat treatment, membrane thickness, and polymer solution concentration on the membrane permeability were evaluated. Pebax® is a highly breathable material, thus its application as breathable chemically-resistant protective clothing was studied. Dimethyl methylphosphonate (DMMP) – a sarin simulant – was selected as the challenge agent. The liquid pervaporation of pure water (simulating perspiration) and pure DMMP were measured for Pebax®1074, Pebax®2533, nitrile, latex, poly(vinyl chloride), low density polyethylene, silicone, and silicone-polycarbonate copolymer under pervaporation mode. Pebax®1074 was not only the most water permeable material but also the most selective of all the tested materials for water/DMMP – making it a very promising material for this application.

Submitted by Johnny Rodrigues (johnnyrodrigues@ufcg.edu.br) on 2018-03-23T18:44:54Z No. of bitstreams: 1 JANAINA RAFAELLA SCHEIBLER - DISSERTAÇÃO PPGEQ 2015..pdf: 2465420 bytes, checksum: cbecc726b67d3d76a334570b655735eb (MD5) / Made available in DSpace on 2018-03-23T18:44:54Z (GMT). No. of bitstreams: 1 JANAINA RAFAELLA SCHEIBLER - DISSERTAÇÃO PPGEQ 2015..pdf: 2465420 bytes, checksum: cbecc726b67d3d76a334570b655735eb (MD5) Previous issue date: 2015 / Entre as membranas inorgânicas microporosas, as membranas zeolíticas constituem uma tecnologia promissora, devido às suas potenciais aplicações normalmente na desidratação do álcool, separação de moléculas de gás, separação de isômeros ou em processos químicos, incluindo reações de esterificação. Sob este aspecto, torna-se imprescindível o estudo das rotas de preparação desses materiais, visando desenvolver produtos com qualidade e a baixo custo. Portanto, a inovação deste estudo se dá na síntese de membranas zeolíticas via método de síntese poreplugging visando a utilização das membranas inorgânicas para permeação gasosa de N2. Neste trabalho foram desenvolvidos os seguintes materiais: zeólita ZSM-5, membranas cerâmicas (γ-alumina e α-alumina) e as membranas zeolíticas (ZSM5/γ-alumina e ZSM-5/α-alumina). A zeólita ZSM-5 foi sintetizada por meio do método hidrotérmico. As membranas cerâmicas (γ-alumina e α-alumina) foram preparadas a partir da técnica de conformação de pós cerâmicos e posteriormente submetidas à sinterização a uma temperatura de 1000 ºC/1h e 1200 ºC/1h respectivamente. A preparação das membranas zeolíticas (ZSM-5/γ-alumina e ZSM-5/α-alumina) foi realizada com base no método pore in plugging. As amostras foram caracterizadas a partir das técnicas de difração de raios X e Microscopia Eletrônica de Varredura. Os resultados experimentais permitem diversas conclusões acerca do desenvolvimento dos materiais: zeólita ZSM-5, membranas cerâmicas (γ-alumina e α-alumina) e membranas zeolíticas (ZSM-5/γ-alumina e ZSM-5/α-alumina). A partir da difração de raios X, foi possível verificar que o método de síntese empregado, foi efetivo na obtenção da zeólita ZSM-5. O difratograma apresentou picos característicos de uma zeólita ZSM-5 quando comparada ao padrão. Os resultados obtidos por DRX para as membranas cerâmicas (γ-alumina e α-alumina) demonstraram a formação de picos característicos do óxido de alumínio, os materiais são cristalinos e puros. Para o método pore-plugging pode se dizer que é um método promissor, pois mostrou uma formação satisfatória da camada zeolítica no resultado do DRX de ambas as membranas zeolíticas (ZSM-5/γ-alumina e ZSM-5/α-alumina). / Among the microporous inorganic membranes, zeolite membranes are a promising technology due to their potential applications normally in alcohol dehydration, separation of gas molecules, separation of isomers or chemical processes, including esterification reactions. In this regard, it is essential to study the preparation of these materials routes in order to develop products with quality and low cost. Therefore, innovation of this study gives the synthesis of zeolite membranes via pore-plugging synthesis method aimed at the use of inorganic membranes for gas permeation N2. In this work the following materials were developed: ZSM-5 zeolite, ceramic membranes (γ-alumina and α-alumina) and zeolitic membranes (ZSM-5/γ-alumina and ZSM-5/α-alumina). Zeolite ZSM-5 was synthesized by the hydrothermal method. Ceramic membranes (γ-alumina and α-alumina) were prepared from the ceramic powder forming technique, and subsequently subjected to a sintering temperature of 1000 °C/1h and 1200 °C/1h respectively. The preparation of zeolite membranes (ZSM-5/γ-alumina and ZSM-5/α-alumina) was carried out based on the method in pore plugging. The samples were characterized from the techniques of X diffraction and scanning electron microscopy rays. The experimental results allow several conclusions about the development of materials: zeolite ZSM-5, ceramic membranes (γ-alumina and α-alumina) and zeolite membranes (ZSM-5/γ-alumina and ZSM-5/αalumina). From the X-ray diffraction, it found that the method of synthesis used was effective in obtaining the zeolite ZSM-5. The XRD pattern showed peaks characteristic of ZSM-5 compared to the standard. The results obtained by XRD ceramic membranes (γ-alumina and α-alumina) showed the formation of peaks characteristic of aluminum oxide, the materials are crystalline and pure. For the poreplugging method can be said to be a promising method because it showed a satisfactory formation of the zeolite layer on the result of XRD both zeolite membranes (ZSM-5/γ-alumina and ZSM-5/α-alumina).

La technologie de Captage et Stockage du CO2 (CSC) est considérée comme une des principales solutions pour limiter les rejets de gaz à effet de serre (CO2) et lutter contre le réchauffement climatique. L’étape de captage fait appel à un procédé de séparation des fumées de post combustion qui a pour fonction l’extraction sélective du CO2 des autres composés. Les principales performances visées sont un taux de capture et une pureté du CO2 supérieurs à 90%, ainsi qu’une consommation énergétique minimale afin de ne pas générer un niveau trop élevé d’émissions secondaires de CO2. La perméation gazeuse par membrane dense est une technologie de séparation potentiellement applicable au captage du CO2 en post combustion. Sur la base de différents types de matériaux et mécanisme de transport associés (processus physique ou chimique) une large plage de valeurs de perméabilité et de sélectivité peut être atteinte. Une des dernières familles de membrane ayant démontrée des performances de séparation pouvant être intéressantes pour le captage du CO2 sont les membranes à transport facilité dites ‘’réactives ‘’. Une analyse systématique des performances de séparation de modules membranaires basés sur des membranes physiques (polymères denses) et sur des membranes réactives (transport facilité) pour le traitement de fumées de post combustion a été réalisée. La simulation d’un procédé de captage complet, incluant un ou deux étages de séparation membranaire, une étape de séchage et une étape de compression a ensuite été effectuée. L’ensemble des résultats, en particulier la pénalité énergétique globale du système et l’estimation des surfaces membranaires nécessaires, permet de positionner la technologie de perméation gazeuse comparativement aux autres procédés de captage / CO2 Capture and Storage (CCS) is a promising solution to separate CO2 from flue gas, to reduce the CO2 emissions in the atmosphere, and hence to reduce global warming. In CCS, one important constraint is the high additional energy requirement of the different capture processes. That statement is partly explained by the low CO2 fraction in the inlet flue gas and the high output targets in terms of CO2 capture and purity (>90%).Gas permeation across dense membrane can be used in post combustion CO2 capture. Gas permeation in a dense membrane is ruled by a mass transfer mechanism and separation performance in a dense membrane are characterized by component’s effective permeability and selectivity. One of the newest and encouraging type of membrane in terms of separation performance is the facilitated transport membrane. Each particular type of membrane is defined by a specific mass transfer law. The most important difference to the mass transfer behavior in a dense membrane is related to the facilitated transport mechanism and the solution diffusion mechanism and its restrictions and limitations.Permeation flux modelling across a dense membrane is required to perform a post combustion CO2 capture process simulation. A CO2 gas permeation separation process is composed of a two-steps membrane process, one drying step and a compression unit. Simulation on the energy requirement and surface area of the different membrane modules in the global system are useful to determine the benefits of using dense membranes in a post combustion CO2 capture technology

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior / A utilização de novos materiais aplicados aos processos de separação por membranas tem sido objeto de constante pesquisa acadêmica e tecnológica. Na permeação de gases petroquímicos, a modificação de estruturas poliméricas e o uso de membranas de transporte facilitado por adição de sais contendo metais ou nanopartículas destacam-se dentre as opções disponíveis. Os objetivos deste trabalho foram avaliar alterações químicas, estruturais e térmicas na matriz polimérica de poli(uretano-ureia) (PUU) provocadas pela adição de nanopartículas de prata (AgNps) e obter dados de pemeabilidade de gases petroquímicos (C2H4, C2H6, CO2 e N2) para avaliar a influência das AgNps no transporte desses gases através do filme polimérico. Alterações nos espectros de FTIR nas bandas de estiramento das ligações C-O-C e C=O (uretânica e ureica), e deslocamentos nos picos de difração, demonstram que houve interação entre as AgNps e o oxigênio éter do PUU. A interação com as AgNps diminuiu a estabilidade térmica dos domínios flexíveis do polímero, região onde são encontrados os grupos éteres. As imagens de TEM mostraram que houve baixa dispersão das Nps na matriz polimérica. A interação das AgNps com o grupo éter diminuiu a permeabilidade de todos os gases, porém a redução da permeabilidade do CO2 e do C2H4 foi muito mais significativa, mostrando a interferência das AgNps na sorção desses dois gases. O transporte facilitado de olefinas através dos filmes poliméricos não foi observado, em parte, causado pela baixa dispersão das AgNps na matriz polimérica. Apesar da interação, não foi possível responder se a superfície das Nps estava ativada para o transporte facilitado. Contudo, através dos resultados do trabalho foi possível propor um mecanismo de interação entre as AgNps e o PUU, e verificar como a presença das Nps pode alterar a interação da matriz polimérica com gases petroquímicos / The use of new materials applied to processes of membrane separation has been the target of constant academic and technological researches. In permeation of petrochemical gases, the modification of polymeric structure to form facilitated transport membranes are one of the worthy available options. In this sense, the goal of this work is, not only evaluate the influence of the addition of silver nanoparticles (AgNps) in the chemical, morphological and thermal properties of poly(urethane urea) (PUU) films, but also obtain permeability data for some petrochemical gases (C2H4, C2H6, CO2 e N2). FTIR spectra exhibited changes in the C-O-C and C=O stretching bands profile of (from urethane and urea groups) and XRD analyses exhibited shifts in peaks. These results demonstrate the AgNps interacted with the ether oxygen of PUU. The interaction with AgNps reduced the thermal stability of polymer soft segments, where the ether linkages are located. TEM images showed a lower dispersion of Np in the polymer matrix. The interaction between AgNps and ether groups also decreased the permeability of all gases. Reduction of CO2 and C2H4 permeability were clear, demonstrating the hindrance of AgNps in the sorption of both gases. The olefin transport facilitated through the polymeric films was not verified. . This is partially caused by the lower dispersion of AgNps in the polymer matrix. Although an interaction between the AgNps and ether oxygen was observed, it was not possible to confirm if the Nps surface was really activated to facilitated transport. However, considering the results obtained it was possible to propose the interaction mechanism between AgNps and PUU; and also to indicate how the presence of Nps can change the interaction between the polymeric matrix and the petrochemical gases

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior / A utilização de novos materiais aplicados aos processos de separação por membranas tem sido objeto de constante pesquisa acadêmica e tecnológica. Na permeação de gases petroquímicos, a modificação de estruturas poliméricas e o uso de membranas de transporte facilitado por adição de sais contendo metais ou nanopartículas destacam-se dentre as opções disponíveis. Os objetivos deste trabalho foram avaliar alterações químicas, estruturais e térmicas na matriz polimérica de poli(uretano-ureia) (PUU) provocadas pela adição de nanopartículas de prata (AgNps) e obter dados de pemeabilidade de gases petroquímicos (C2H4, C2H6, CO2 e N2) para avaliar a influência das AgNps no transporte desses gases através do filme polimérico. Alterações nos espectros de FTIR nas bandas de estiramento das ligações C-O-C e C=O (uretânica e ureica), e deslocamentos nos picos de difração, demonstram que houve interação entre as AgNps e o oxigênio éter do PUU. A interação com as AgNps diminuiu a estabilidade térmica dos domínios flexíveis do polímero, região onde são encontrados os grupos éteres. As imagens de TEM mostraram que houve baixa dispersão das Nps na matriz polimérica. A interação das AgNps com o grupo éter diminuiu a permeabilidade de todos os gases, porém a redução da permeabilidade do CO2 e do C2H4 foi muito mais significativa, mostrando a interferência das AgNps na sorção desses dois gases. O transporte facilitado de olefinas através dos filmes poliméricos não foi observado, em parte, causado pela baixa dispersão das AgNps na matriz polimérica. Apesar da interação, não foi possível responder se a superfície das Nps estava ativada para o transporte facilitado. Contudo, através dos resultados do trabalho foi possível propor um mecanismo de interação entre as AgNps e o PUU, e verificar como a presença das Nps pode alterar a interação da matriz polimérica com gases petroquímicos / The use of new materials applied to processes of membrane separation has been the target of constant academic and technological researches. In permeation of petrochemical gases, the modification of polymeric structure to form facilitated transport membranes are one of the worthy available options. In this sense, the goal of this work is, not only evaluate the influence of the addition of silver nanoparticles (AgNps) in the chemical, morphological and thermal properties of poly(urethane urea) (PUU) films, but also obtain permeability data for some petrochemical gases (C2H4, C2H6, CO2 e N2). FTIR spectra exhibited changes in the C-O-C and C=O stretching bands profile of (from urethane and urea groups) and XRD analyses exhibited shifts in peaks. These results demonstrate the AgNps interacted with the ether oxygen of PUU. The interaction with AgNps reduced the thermal stability of polymer soft segments, where the ether linkages are located. TEM images showed a lower dispersion of Np in the polymer matrix. The interaction between AgNps and ether groups also decreased the permeability of all gases. Reduction of CO2 and C2H4 permeability were clear, demonstrating the hindrance of AgNps in the sorption of both gases. The olefin transport facilitated through the polymeric films was not verified. . This is partially caused by the lower dispersion of AgNps in the polymer matrix. Although an interaction between the AgNps and ether oxygen was observed, it was not possible to confirm if the Nps surface was really activated to facilitated transport. However, considering the results obtained it was possible to propose the interaction mechanism between AgNps and PUU; and also to indicate how the presence of Nps can change the interaction between the polymeric matrix and the petrochemical gases

The implementation of polymer membranes in gas separation applications has been investigated to a great extent. Nevertheless, only a few types of polymers are used in commercial applications, disclosing the need for new materials with superior membrane performance to make membrane processes a more competitive technology over the conventional ones. Based on this context, this work focuses on the development of new polymeric membranes. Polyaniline (PANI), a multifaceted polymer that can change its structural properties upon various modification procedures, was chosen as membrane material. PANI membranes possess attractive O2/N2 selectivities, wherefore it is an interesting candidate for the use in gas separation applications, such as generation of oxygen-enriched air or inert gas generation. However, membranes made from neat PANI are suffering from brittleness and thus create leak paths through the membrane. Therefore PANI was blended with polybenzimidazole (PBI), a temperature stable polymer with good film-forming properties facilitating the preparation of thin, stable polymer films. Furthermore, several techniques were investigated including acid-doping, thermal treatment, and addition of titanate nanotubes (TiNTs) to enhance the separation properties. The materials that have been prepared are: 1)...

The objectives of this research were to study the gas transport properties of proton exchange membranes (PEM), namely disulfonated poly(arylene ether sulfone) (BPSH-35), post sulfonated diels-alder poly(phenylene) (SDAPP), and poly(perfluoro sulfonic acid) (Nafion). The O2 gas permeabilities were found to be lower in BPSH and SDAPP as compared to poly(perfluoro sulfonic acid) because of difference in Tg (TgBSPH= 250 oC, TgSDAPP= 330 oC versus TgNafion=150 oC). Higher Tg polymers have a more rigid, inflexible polymer segments causing a reduction in gas permeability. In comparison to SDAPP, BPSH has a lower O2 gas permeability because of the bulky side groups in the SDAPP backbone. O2 sorption measurements were carried out both under non-humidified and humidified conditions as a function of relative humidity and temperature at a normal PEM operating pressure of 1 atm. Under non-humidified conditions, BPSH, SDAPP, and Nafion 112 exhibited Henry's Law sorption, consistent with dilute dissolution of O2 into the polymer matrix. The enthalpies of sorption were calculated to determine the interaction of O2 with each membrane. The sorption enthalpies in BPSH and SDAPP increased with increasing pressure indicating the formation of more O2-O2 interactions. The enthalpies in Nafion 112 were relatively constant with increasing pressure. In the presence of moisture, the sorption behavior changed from Henry's Law to Type IV sorption behavior, which is common in hydrophilic polymers. The SDAPP membrane was found to have the highest percent wet O2 mass uptake because of a higher number of sulfonic acid groups interacting with the water/O2 system. Finally the O2 sorption for various porous catalyst powders, consisting of platinum supported on carbon was measured in the non-humidified and humidified state. The catalysts were found to have Knudsen diffusion in the non-humidified state with 20 wt% Pt-C having the largest O2 sorption. In the humidified state, the highest O2 mass uptake was achieved with 40 wt% Pt-C. These results are explained in terms of the trade-off between catalyst dispersion and catalyst size. Furthermore, O2 sorption measurements were utilized for membrane electrode assemblies containing 40 wt% Pt-C and hot pressed at 210 oC for BPSH-35 (25 and 80K) and Nafion 112 membranes. The same sorption behavior occurred in the MEAs as in the neat membrane, but at a lower capacity. This is because the electrode introduces a more tortuous path to the gas molecules permeating across the membrane. / Ph. D.

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior / Entre os polímeros considerados promissores para a remoção seletiva de CO2, destacam-se aqueles que contêm os grupos glicol etilênico (EG). Nesta dissertação, foram obtidos filmes a partir de dispersões aquosas de poliuretano (PU), sintetizadas em trabalho anterior, à base de poli(glicol propilênico) (PPG), copolímero em bloco à base de poli(glicol etilênico) (PEG) e PPG (EG-b-PG), ácido dimetilolpropiônico (DMPA), diisocianato de isoforona (IPDI) e etilenodiamina (EDA). PPG, EG-b-PG e DMPA formaram as regiões flexíveis nas proporções de: PPG 100% e 0% EG-b-PG, PPG 75% e 25% EG-b-PG, PPG 50% e 50% EG-b-PG e PPG 25% e 75% EG-b-PG em termos de equivalentes-gramas. A influência da quantidade dos segmentos de PEG foi avaliada por ensaios de permeação com os gases CO2, CH4 e N2. Os filmes obtidos das dispersões foram caracterizados por espectrometria de infravermelho com transformadas de Fourier (FTIR), análise termogravimétrica (TGA), difração de raios x (DRX) e espalhamento de raios X a baixo ângulo (SAXS). Espectros de FTIR mostraram que os segmentos de EG influenciaram a frequência da banda de carbonila. Curvas de perda de massa (TG) mostraram perfis semelhantes de degradação, enquanto que as curvas derivadas apresentaram diferenças. DRX e SAXS mostraram que os segmentos de PEG promoveram uma maior ordenação na estrutura da membrana. Testes de permeação de gases mostraram que o aumento do teor de PEG aumentou o valor da permeabilidade para o CO2, indicando que os segmentos de PEG interagiram favoravelmente com este gás. Em relação ao CH4 e N2, houve uma diminuição na permeabilidade quando comparados com os valores encontrados para o CO2, sendo atribuído a perda de mobilidade segmental. Em termos de seletividade, para o par CO2/CH4 foi obtido um valor médio de 61,7 para a membrana contendo o maior teor de PEG, e o par CO2/N2 um valor médio de 121,5, sendo superior aos valores encontrados na literatura, tornando o material promissor / Among the polymers considered promising for the selective removal of CO2 from natural gas, those containing ethylene glycol groups (EG) are the most distinguished. In this study cast films were obtained from aqueous dispersions of polyurethane (PU), synthesized in a previous work with poly (propylene glycol) (PPG), block copolymer based on poly(ethylene glycol) (PEG) and PPG, dimethylolpropionic acid (DMPA), isophorone diisocyanate (IPDI) and ethylenediamine (EDA). Segments of PPG, EG-b-PG and DMPA formed the flexible domains in the proportions of: PPG 100% and 0% EG-b-PG, PPG 75% and 25% EG-b-PG, PPG 50% and 50% EG-b-PG and PPG 25% and 75% EG-b-PG, in terms of equivalent-grams. The influence of the amount of PEG segments in permeation properties of CO2, CH4 and N2 was verified by permeability essays. The membranes were obtained as cast films from the dispersions and was characterized by infrared spectrometry (FTIR), termogravimetric analysis (TGA), X ray diffractometry (XRD) and small angle X ray scattering (SAXS). FTIR spectra showed that PEG segments influenced carbonyl band frequency. Loss of mass curves with temperature (TG) showed similar profiles of degradation, whereas DTG curves presented more stages. PEG segments conferred higher thermal stability for the materials. XRD and SAXS analysis showed that PEG promoted ordination to the membranes. In gas permeation tests, it was verified that the increase in copolymer amount increased permeability value for CO2, being attributed to the fact that the segments of poly(ethylene glycol) interacted favorably with this gas. In relation to CH4 and N2, there was a significant decrease in permeability when compared to the values found for CO2, being assigned to a loss of segmental mobility with increasing content of EG. In terms of selectivity, the pair CO2/CH4 had a mean value of 61,7 for the membrane containing the highest amount of EG groups, and the pair CO2/N2 produced a mean value of 121,5 for the same one, being superior than those found in the literature, making a promising material

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior / Entre os polímeros considerados promissores para a remoção seletiva de CO2, destacam-se aqueles que contêm os grupos glicol etilênico (EG). Nesta dissertação, foram obtidos filmes a partir de dispersões aquosas de poliuretano (PU), sintetizadas em trabalho anterior, à base de poli(glicol propilênico) (PPG), copolímero em bloco à base de poli(glicol etilênico) (PEG) e PPG (EG-b-PG), ácido dimetilolpropiônico (DMPA), diisocianato de isoforona (IPDI) e etilenodiamina (EDA). PPG, EG-b-PG e DMPA formaram as regiões flexíveis nas proporções de: PPG 100% e 0% EG-b-PG, PPG 75% e 25% EG-b-PG, PPG 50% e 50% EG-b-PG e PPG 25% e 75% EG-b-PG em termos de equivalentes-gramas. A influência da quantidade dos segmentos de PEG foi avaliada por ensaios de permeação com os gases CO2, CH4 e N2. Os filmes obtidos das dispersões foram caracterizados por espectrometria de infravermelho com transformadas de Fourier (FTIR), análise termogravimétrica (TGA), difração de raios x (DRX) e espalhamento de raios X a baixo ângulo (SAXS). Espectros de FTIR mostraram que os segmentos de EG influenciaram a frequência da banda de carbonila. Curvas de perda de massa (TG) mostraram perfis semelhantes de degradação, enquanto que as curvas derivadas apresentaram diferenças. DRX e SAXS mostraram que os segmentos de PEG promoveram uma maior ordenação na estrutura da membrana. Testes de permeação de gases mostraram que o aumento do teor de PEG aumentou o valor da permeabilidade para o CO2, indicando que os segmentos de PEG interagiram favoravelmente com este gás. Em relação ao CH4 e N2, houve uma diminuição na permeabilidade quando comparados com os valores encontrados para o CO2, sendo atribuído a perda de mobilidade segmental. Em termos de seletividade, para o par CO2/CH4 foi obtido um valor médio de 61,7 para a membrana contendo o maior teor de PEG, e o par CO2/N2 um valor médio de 121,5, sendo superior aos valores encontrados na literatura, tornando o material promissor / Among the polymers considered promising for the selective removal of CO2 from natural gas, those containing ethylene glycol groups (EG) are the most distinguished. In this study cast films were obtained from aqueous dispersions of polyurethane (PU), synthesized in a previous work with poly (propylene glycol) (PPG), block copolymer based on poly(ethylene glycol) (PEG) and PPG, dimethylolpropionic acid (DMPA), isophorone diisocyanate (IPDI) and ethylenediamine (EDA). Segments of PPG, EG-b-PG and DMPA formed the flexible domains in the proportions of: PPG 100% and 0% EG-b-PG, PPG 75% and 25% EG-b-PG, PPG 50% and 50% EG-b-PG and PPG 25% and 75% EG-b-PG, in terms of equivalent-grams. The influence of the amount of PEG segments in permeation properties of CO2, CH4 and N2 was verified by permeability essays. The membranes were obtained as cast films from the dispersions and was characterized by infrared spectrometry (FTIR), termogravimetric analysis (TGA), X ray diffractometry (XRD) and small angle X ray scattering (SAXS). FTIR spectra showed that PEG segments influenced carbonyl band frequency. Loss of mass curves with temperature (TG) showed similar profiles of degradation, whereas DTG curves presented more stages. PEG segments conferred higher thermal stability for the materials. XRD and SAXS analysis showed that PEG promoted ordination to the membranes. In gas permeation tests, it was verified that the increase in copolymer amount increased permeability value for CO2, being attributed to the fact that the segments of poly(ethylene glycol) interacted favorably with this gas. In relation to CH4 and N2, there was a significant decrease in permeability when compared to the values found for CO2, being assigned to a loss of segmental mobility with increasing content of EG. In terms of selectivity, the pair CO2/CH4 had a mean value of 61,7 for the membrane containing the highest amount of EG groups, and the pair CO2/N2 produced a mean value of 121,5 for the same one, being superior than those found in the literature, making a promising material